ML12234A252: Difference between revisions
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I i INSIDE EDG CELL I | I i INSIDE EDG CELL I | ||
D \FOUTSIDE | D \FOUTSIDE | ||
" ID ""-,- , SOUNDING TUBE m | " ID ""-,- , SOUNDING TUBE m | ||
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Latest revision as of 13:40, 6 February 2020
ML12234A252 | |
Person / Time | |
---|---|
Site: | Indian Point ![]() |
Issue date: | 02/14/2012 |
From: | Hill J, Schimpf R, Shepard B Entergy Nuclear Northeast |
To: | Office of Nuclear Reactor Regulation |
References | |
NL-12-097 IP3-CALC-EG-00217 | |
Download: ML12234A252 (80) | |
Text
ENCLOSURE 2 TO NL-12-097 IP-CALC-EG-00217, "EMERGENCY DIESEL GENERATOR STORAGE TANK LEVEL SETPOINTS," REV. 5 ENTERGY NUCLEAR OPERATIONS, INC.
INDIAN POINT NUCLEAR GENERATING UNIT NO. 3 DOCKET NO. 50-286
ATTACHMENT 9.2 ENGINEERING CALCULATION COVER PAGE F1 ANO-1 5 ANO-2 El GGNS El IP-2 0 IP-3 5 PLP 5JAF ElPNPS [I RBS D VY El W3 El NP-GGNS-3 El NP-RBS-3 CALCULATION (1) EC # 32406 (2)Page I of 74 COVER PAGE (3) Design Basis Caic. H YES El NO (4) [" CALCULATION I* EC Markup
ý5) Calculation No: iP3-CALC-EG-00217 *") Revision: 5 (7)
Title:
Emergency Diesel Generator Storage Tank Level Setpoints Editorial E
__ YES 0 NO (9) System(s): EDG (Fuel Oil) (10) Review Org (Department): Design i&C (11) Safety Class: (12) Component/EquipmentlStructure Type/Number:
Z Safety / Quality Related LC-1 204S LI-1 133 LC-1207S E- Augmented Quality Program El Non-Safety Related LC-1 205S L-1i 134 LC-1208S LC-1206S LI-1135 LC-1209S (13) Document Type: Calc EDG-31-FO-STNK EDG-31-FO-DTNK (14) Keywords (DescriptionlTopical EDG-32-FO-STNK EDG-32-FO-DTNK Codes):
EDG, Fuel Oil, Level Switches EDG-33-FO-STNK EDG-33-FO-DTNK Level Indication, Day tank (15) Name/Signature/Date e/oigyature/Date e INan /k (17) N 4me/Signature/Date Robert Schi .1i Bruce Shepard John Hill RegsponsjiJe Engineer [ Design Verifier SupervisorlApproval
- Reviewer E] Comments Attached El Comments Attached
/
EN-DC-126 REV 4
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 2 of 74 ATTACHMENT 9.3 CALCULATION REFERENCE SHEET CALCULATION CALCULATION NO: IP3-CALC-EG-00217 REFERENCE SHEET REVISION: 5 I. EC Markups Incorporated (N/A to NP calculations)
- 1. NONE 2.
3.
4.
II. Relationships: Sht Rev Input Output Impact Tracking Doc Doc Y/N No.
- 1. IP-CALC-1 1-00058 "1 0] 0_
- 2. IP-CALC-11-00011 0 0 0_
- 3. IP-RPT-09-00014 1 El N
- 4. 3-SOP-EL-009 E3 [E Y 5.3-SOP-EL-001 0 '_ _ y
- 6. ESOMS (log readings) El 0] Y
- 7. 3-PT-R 160NB/C (3 0] Y III. CROSS
REFERENCES:
- 1. NONE 2.
3.
4.
5.
IV. SOFTWARE USED:
Title:
NONE Version/Release: Disk/CD No.
V. DISK/CDS INCLUDED:
Title:
NONE Version/Release Disk/CD No.
V*I. OTHER CHANGES:
NONE EN-flC-i~r Prf, A
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 3 of 74 ATTACHMENT 9.4 RECORD OF REVISION Sheet I of I Revision Record of Revision SUPERSEDES IP3-CALC-EG-00217 REV 3 4
SUPERSEDES IP3-CALC-EG-00217 REV 4 5 Removes the various EDG loading scenarios & usage calculations and adds reference to Mechanical EDG fuel oil usage calculation. General revision of all sections of the calculation.
EN-DC-126 RFV A
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 4 of 74 TABLE OF-CONTENTS SECTION DESCRIPTION PAGE Table of Contents ............................................................................................................................ 4 1.0 PURPO SE ...................................................................................................................................... 5 2.0 ASSUM PTIO NS .............................................................................................................................. 5 3.0 REFERENC ES ............................................................................................................................... 7 4.0 ATTACHM ENTS ............................................................................................................................. 9 5.0 LO OP FUNCTIO N ........................................................................................................................ 10 6.0 BLO CK DIAG RAM ........................................................................................................................ 12 7.0 UNCERTAINTY EQ UATIONS ................................................................................................ 13 8.0 MO DULE UNCERTAINTY (en) ................................................................................................ 15 9.0 CALCULATE CHANNEL UNCERTAINTY (CU) ....................................................................... 18 10.0 EDG TANKS ................................................................................................................................. 20 11.0 ANALYTICAL LIMIT (AL) OR NOMINAL PROCESS LIMIT (NPL) .......................................... 24 12.0 DETERM INE SETPO INT (TS) ................................................................................................. 27 13.0 DETERM INE AS FO U ND VALU E (AFV) ............................................................................ 30 14.0 SUM MARY .................................................................................................................................... 31 15.0 EDG F.O. STORAGE TANK FIELD CALIBRATION CONSIDERATIONS ............................... 33 TABLE 1 - Slope Effect on Measurements for EDG Fuel Oil Storage Tanks No. 31, 32 & 33 ................... 35, 36, 37 Attachments Pages 1 ........................................................................................................................................... DELETED - 0 pages 2 ............................................................................................................................................................... 2 pages 3 ................................................................................................................................................................. 1 page 4 ................................................................................................................................................................. I page 5 ............................................................................................................................................................... 1 page 6 ........................................................................................................................................... DELETED - 0 pages 7 ........................................................................................................................................... DELETED - 0 pages 8 ........................................................................................................................................... DELETED - 0 pages 9 ........................................................................................................................................... DELETED - 0 pages 10 ................................................................................................................................................................. 1 page 11 ........................................................................................................................................... DELETED - 0 pages 12 ............................................................................................................................................................. 15 pages 13 ............................................................................................................................................................... 2 pages 14 ............................................................................................................................................................... 3 pages 15 ............................................................................................................................................................. 11 pages Total: 74 pages
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 5 of 74 1.0 PURPOSE 1.1. This calculation identifies the Channel uncertainty and the appropriate settings for the EDG Underground Fuel Oil Storage Tank (FOST) Level Switches (LS), (LC-1204S, LC-1205S &
LC-1 206S). The switches provide:
" LOW - Alarm function and
" LOW-LOW - Stop the fuel oil transfer pumps at low-low oil level to protect them from effects of vortexing or inadequate NPSH.
1.2 This calculation identifies the uncertainty for EDG Underground Fuel Oil Storage Tank Level Indicators (LI-1 133, LI-1 134 & LI-1 135) and the dipstick readings (level indication by sounding tank). Table 1 (attached) identifies Tank slope effect on Setpoint, volume, and sounding tube measurements.
1.3. This calculation uses EDG Day Tank level switches (LC-1 207S, LC-1 208S & LC-1 209S) actuation points to document storage considerations.
NOTE: Revision 5 is a major revision. Therefore it is not practical to identify each line change. This revision supersedes Revision 4 which is available from records for comparing any changes and previous calculation results.
2.0 ASSUMPTIONS 2.1 The displacer trip level sheets from Magnetrol have 100°F as the lowest temperature listed, although certification lists temperature range as 35 0 F-1 10F. Tanks are underground, and temperature variations are assumed to be minimal. Extrapolation down to 30°F is based on data points at 100IF and 200 0 F. Function with respect to process temperature is assumed to be linear over this range (see attachment 4.2). The 30°F temperature is considered conservative based on Attachment 4.10 & 4.14. Additionally, it is considered conservative to evaluate the uncertainty associated with temperature effect (TE) based on a postulated nominal calibration temperature of 70 °F with temperature excursions between 30°F and 110°F or +/-40 OF. This span is considered conservative based on the specified span of 35 0 F to 1 10°F (see attachments 4.2, 4.10 & 4.14).
2.2 Oil displaced by equipment/hardware installed inside the tank is considered negligible.
2.3 It is assumed conservative to interpolate values by Lagrange's Interpolation formula using a minimum of six known values about the unknown. The values for volume and inches in Table 1 were interpolated using this methodology, based upon Ref. 3.2. Values used in this calculation which are not in the table were linearly interpolated from adjacent table values.
2.4 The effects of normal vibration (or a minor seismic event that does not cause an unusual event) on the level switches is assumed to be dampened out by the fluid surrounding the displacers and; therefore seismic effects (SE) are considered to be negligible. For post-accident operability considerations, it is noted that a design basis accident coincident with a design basis earthquake is not postulated. It is assumed that following a SSE seismic event the setpoint of the Magnetrol switches and Uehling indicator readings cannot be warranted until the instrumentation has been functionally evaluated and subjected to a calibration check. Additionally, it is assumed that Magnetrol switch contacts may chatter causing a false alarm or pump start/stop signal during, but not following, a SSE.
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 6 of 74 2.5 For a displacer type level switch, based upon Engineering Judgment, it is assumed the As-Left-Tolerance will be _ 2.4 x RA (Where RA is the reference accuracy of the device).
2.6 This calculation uses fuel oil specific gravity of 0.83 for all settings, unless stated otherwise.
2.7 Fuel specific gravity is maintained between 0.83 and 0.89 (see attachment 4.5). Volume required in tank has previously been calculated in gallons (Ref. 3.10 & 3.21) at lowest density (0.83 specific gravity) to maximize required volume. The evaluation in Ref. 3.10 identifies that as specific gravity increases the required volume for operation at any specific load decreases. Review of the adjusted low (net) heat values in BTUs per gallon and BTUs per LB for the range of allowed fuel density indicates that as the density is increased, BTUs per gallon increases, and the required volume for any specific load would decrease.
2.8 The conversion from gallons to inches in Table 1 is not based on volume measurements.
The conversion basis is found in Calculation 200 (Ref. 3.2). Tank tilt has negligible effect on volume measurements.
2.9 Inch values of calculations will be rounded-off to 5 / 1 0 0 th (0.05) of an inch.
2.10 Final gallon values of calculations will be rounded-off to whole gallons.
2.11 This calculation assumes normal plant operating conditions (non-seismic/non-harsh environment).
2.12 Magnetrol displacer (float) calculations are from the available manufacturer information (Magnetrol installation drawing, see attachment 4.2). Actual performance of displacers versus design settings was field verified (see attachment 4.15).
2.13 The Level Indicators LI-1 133, LI-1 134 & LI-1 135 (manometer/bubbler) are calibrated for a liquid specific gravity (SG) of 0.86 based on attachment 4.12. It should be noted that SG less then 0.86 is acceptable since the read indication would be lower then the actual tank level and more than required (Indication would be conservative). Additionally, it should be noted that SG above 0.86 is considered conservative due to the increase in BTU/gallon (see reference 3.21) and indicator SG allowance. NOTE: Presently the Operations Graphs TC-25B & D show a correction factor for SG change (see Attachment 4.12).
2.14 Tank coating reduces usable tank volume by less than 20 gallons, based upon engineering judgment, since:
- tank coating was identified to reduce total tank volume by -25 gallons (ref. 3.2),
- <82% of the tank heads coating material is in the usable volume area, and heads are less than 24% of the total surface area of the tank,
- <40% of the cylinder tank coating material is in the usable volume area [107.5" diameter cylinder portion of tank, 'A of surface area is below 15.7" elevation (and floor is twice as thick), and 14 is above the 91.5" elevation], 76% of the total surface area of the tank,
- <58% of the total tank coating material is in the usable volume area.
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 7 of 74
3.0 REFERENCES
3.1 ISA-RP67.04, Part I1,"Methodologies for the Determination of setpoints for Nuclear Safety-Related Instrumentation", dated September 1994.
3.2 IP3-TS-200 calculation "Diesel Generator Fuel Oil Storage Tanks Capacity Calculation",
dated 1/19/90, (Including Margin Rev. 0A dated 10/01/1999).
3.3 EN-IC-S-01 0-MULTI, Instrument Loop Accuracy and Setpoint Calculation Methodology.
3.4 Technical Specification 3.8.1 "AC Sources - Operating".
3.5 Technical Specification 3.8.3 "Diesel Fuel Oil and Starting Air".
3.6 Final Safety Analysis Report (FSAR),
3.7 Drawings
(1) 9321-F-20303, "Flow Diagram Fuel Oil to Diesel Generators".
(2) IP3V-0353-0002 (FP 9321-05-2990), "Fuel Oil Storage Tank (7700 GAL)".
(3) IP3V-0186-0043 & IP3V-0186-0046 (FP 9321-05-20324 sheets 1 & 2), "Outline Model VITX-5D, 3X6JLC 4 Stage".
3.8 EN-DC-1 26, Revision 4, Engineering Calculation Process 3.9 EN-DC-1 15, Revision 12, Engineering Change Process 3.10 IP-CALC-1 1-00058, Revision 1, IP3 Emergency Diesel Generator (EDG) Fuel Oil Consumption Licensing Basis Calculation.
3.11 Preventive Maintenance Procedure "Diesel Generator Fuel Oil Storage Tank NO. 31 Level Indicator", IC-PM-LI-1133, 1134 & 1135.
3.12 Modification MMP 94-3-132, "EDG Fuel Oil Tank Level Indicator LI-1 133, LI-1 134, LI-1 135 Replacement, "dated 10/21/94.
3.13 Alarm Response Procedures, 3-ARP-011, "Panel SHF - Electrical", Rev. 34.
3.14 WR No. 94-03803-3 "DG F.O. Storage Tank 31 Level", dated 8/8/94. Implements IP3 SCR-94-010, 8/9/94, Change Low & Low-Low settings on level switch (LC-1204S) 3.15 WR No. 94-03803-14 "DG F.O. Storage Tank 32 Level", dated 11/30/94. Implements IP3 SCR-94-026, 10/28/94, Change Low & Low-Low settings on level switch (LC-1 205S) 3.16 WR No. 94-03803-11 "OG F.O. Storage Tank 33 Level", dated 11/15/94. Implements 1P3 SCR-94-027, 10/28/94, Change Low & Low-Low settings on level switch (LC-1206S)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 8 of 74 3.17 IP-3 Calculation 204 "Diesel Generator Fuel Oil Consumption," dated 2/6/90.
3.18 System Operating Procedures, 3-SOP-EL-009 "Filling the Diesel FOST's" Rev. 20.
3.19 Plant Equipment Database in Asset Suite (1AS) 3.20 Periodic Testing of Diesel Generator Units Used as Onsite Electric Power Systems at Nuclear Power Plants, REG GUIDE 1.108, 1977 3.21 IP-CALC-1 1-00011, Revision 0, Evaluation of Emergency Diesel Generator (EDG) Fuel Oil Usages Accounting for Issues identified During the IP3 2010 NRC CDBI.
3.22 0-CY-1 810 Rev. 11, Diesel Fuel Oil Monitoring, Chemistry Procedure 3.23 IP-RPT-09-00014, Rev. 1, Critical Submergence Evaluation Related to Surface Vortices in Nuclear Safety and Augmented Quality Tanks/Pumps at IPEC
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 9 of 74 4.0 ATTACHMENTS 4.1 DELETED 4.2 Magnetrol Drawing D-1257 (FP 9321-05-7214 Rev. 0, 1/22/70) "Magnetrol Installation Dimensions Model A-153-F-TDM & A-153-F-E.P.-TDM" 4.3 Gould Pumps Bowl Engineering Data, Document # 22.13, October 1, 1986, "Minimum Submergence Required for Vortex Suppression".
4.4 Telephone Discussion Documentation form, 6/5/91, A. Cerwin to T. Fricke.
4.5 Telephone Discussion Documentation form, 11/10/93, F. Granitto to D. Wilson.
4.6 DELETED 4.7 DELETED 4.8 DELETED 4.9 DELETED 4.10 U.S. Environmental Protection Agency (EPA), 1995, Review of MathematicalModeling for Evaluating Soil Vapor Extraction Systems, Office of Research and Development, Washington, D.C. EPA/540/R-95-513 - Figure 1. "Average Shallow Ground Water Temperature in the United States" 4.11 DELETED 4.12 IP3-RPT-EDG-01632, "Operation Graphs, TC-25A through TC-25D Diesel Generator Fuel Oil Storage Tanks Slope and Specific Gravity Compensation, "dated 10/21/95.
4.13 FAX MESSAGE, from A.E. Vazquez of Uehling, to R.F. Jones of MDM Engineering, "Certificate of Calibration" dated 12/18/95.
4.14 Specification for "Liquid Level Switches", No. 9321-05-252-20, Revision 2, Pages 3, 4 & 5, dated 9/19/95.
4.15 Telecopy Transmittal Sheet IP3, To R. JONES (I&C), From M. Pactong (Mech Eng), dated 12/1/95.
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 10 of 74 5.0 LOOP FUNCTION 5.1 General There are 3 EDG Underground Fuel Oil Storage Tanks (FOST). Each tank has three level indication/monitoring devices or capabilities. Functions considered within the scope of this calculation are; LOW & LOW-LOW tank level switch (Displacer Type), tank level indicator (Manometer/Bubble type) and level indicator (Dipstick). The instrumentation is further described below:
5.2 Level Switches (LC-1204S, LC-1205S, & LC-1206S)
Each EDG Underground Storage Tank has one Magnetrol Level Switch (LS), with separate actions for one control circuit and one alarm circuit on each Magnetrol LS. Each LS has two (2) setpoints which actuate on decreasing tank level. The low (LOW) level setting on each tank actuates a CCR alarm; alerting operators that action to replenish the storage tank volume is required. Level switch actuation at the low-low (LOW-LOW) level stops the Underground Fuel Oil Storage Tank transfer pump to provide protection from vortexing or inadequate NPSH. The LOW and LOW-LOW LS setpoints for each tank envelope the volume of fuel oil required for specified EDG operation.
The LS's are Magnetrol model A-153-FTDM (Reference 3.19). They use 2 Karbate displacers that operate two DPDT micro-switches. The specified service is #2 diesel fuel oil, atmospheric pressure, at 350 - 1 100 F; specific gravity 0.84 to 0.89. They have tag numbers of LC-1204S, LC-1205S & LC-1206S for tanks 31, 32 & 33 respectively. There is one device in each tank. Each device controls two circuits. Each circuit operates from an independent micro-switch. One switch is in the control circuitry for the pump motor, the other actuates a CCR alarm. See Attachments 4.2 and 4.14.
5.3 Level Indicators (LI-1-133, LI-1134 & LI-1135)
The Level Indicators (LI's) provide the following functions:
(1) Indication of tank level, (2) Provide an indication of tank leakage (In-Leakage, Out-Leakage) and (3) Following an event, which requires EDG operation, the indicators provide indication of tank level approaching the FOST transfer pump STOP setpoint.
The LI's are located in the cell for each EDG and provide FOST tank level readout. The LI's are Uehling Instrument Co. model 55R173 (Reference 3.19). They consist of a manometer (with readout), a pneumatic hand pump (for air supply), and a dip tube (process interface bubbler). When the hand pump is operated a flow of air passes through tubing to the dip tube; when air bubbles escape from the submerged open end, the air pressure in the tube equalizes to the hydrostatic head of the tank fuel oil. As the tank fuel oil head varies, the air pressure in the dip tube changes correspondingly. The air pressure is indicated on the manometer in inches and equivalent gallons. The manometer and hand pump are located in each EDG cell. The dip tube is located in each underground storage tank. The manometer fill fluid is Diazene-42. The specified service is #2 diesel fuel oil, atmospheric pressure at 350 - 110°F; specific gravity 0.86. They have tag numbers of LI-1 133, LI-1 134 & LI-1 135 for tanks 31, 32 & 33 respectively. There is one device in each tank. Operations Graph TC-25B and TC-25D show the relationship between level in inches and gallons.
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 11 of 74
. 5.4 Dipstick Each EDG FOST has a specific location for sounding the tank with a Dipstick, the sounding tube. The Dipstick is stored near the sounding tubes for the underground storage tanks. The Dipstick has markings in inches. Manual measurements are made at the sounding tube location for each tank. The specified service is for the EDG fuel oil (#2 diesel) storage tanks.
No tag number is associated with the Dipstick. There is one Dipstick for the three EDG tanks. Operations Graph TC-25A and TC-25C show the relationship between level in inches and gallons for each tank. Additionally the relationship between Sounding tube measurement and each tank volume was documented in IP3-RPT-EDG-01632, and is shown in Table 1 of this calculation.
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 12 of 74
. 6.0 BLOCK DIAGRAM 1 CC LO _LO LO LI un I Ir(
-.. ........ 1 0.LI...
. *. .. n ........
- ---N AIR SUPPLY F7 - -,
I i INSIDE EDG CELL I
D \FOUTSIDE
" ID ""-,- , SOUNDING TUBE m
V SLOPE DOWN See Reference 3.7(2) for tank dimensions and specific device locations DEVICE EDG TK 31 EDG TK 32 EDG TK 33 NOTE:
LC SWITCH LC-1204S LC-1205S LC-1206S e, for LOW-LOW &e2 for LOW LVL LI INDICATOR LI-1 133 LI-1 134 LI-1 135 e 6&7 for LOW-LOW & e 4&sfor LOW LVL LE ELEMENT YES YES YES N/A SOUND TUBE YES YES YES e3 (for DIPSTICK)
FIGURE 1 LOOP DIAGRAM TYPICAL
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 13 of 74
- 7.0 UNCERTAINTY EQUATIONS CU = +/-(PM2 +PE 2 +e1 2 +e 22 +... +e 2 +IRE 2)11 2 +/-B Where, 2 2 2 2 2 e = +/-(RA +DR +TE +RE +SE +HE 2 +PS 2 +ALT 2 +SP 2 +MTE 2) 1 2 +/-B 7.1 Uncertainty terms taken to be either negligible or not applicable (not included elsewhere in the evaluation) are:
- IRE - Mild environment & switches are OFF-ON not analog, therefore, IRE is not applicable
- B - No process or module bias identified, therefore, relative to the magnitude of known uncertainties, any bias that may be inherent in the loops is considered to be negligible (The effects of slope are accounted for in scaling for each tank)
- RE - Non-radiological environment, therefore, RE is not applicable
- HE - Humidity changes are within the operating range of the devices and are considered to be negligible
- PS - The switch is an OFF-ON device not analog and is not affected by power supply changes O
- SP - The tanks are at atmospheric pressure, therefore, any static pressure effect is negligible 7.2 Uncertainty Allowances to Address (1) PM - Process Measurement Effect (2) e, - Equipment Uncertainties (3) ALT or CT - Calibration Uncertainties (4) Other Uncertainties 7.2.1 Process Measurement effects (PM)
Fuel oil may be supplied at various SGs of 0.83 to 0.89 (Ref. 3.22). The Chemistry Supervisor at IP3, responsible for the fuel oil monitoring data, indicated that the average SG of existing fuel oil is 0.84 SG and does not vary significantly when new fuel is added to the storage tanks (See Attachment 4.5). Chemistry testing identified the following EDG FOST density values based upon field testing, which are numerically equivalent to SG values 11/18/11 - 31 EDG FOST - 0.8482 grams/ml = SG of 0.8482 11/18/11 - 32 EDG FOST - 0.8449 grams/ml = SG of 0.8449 11/18/11 - 33 EDG FOST - 0.8482 grams/ml = SG of 0.8482 Ref. 3.10 identified Btu/LB, Btu/Gal, and required fuel gallons calculated at various SG between 0.83 & 0.89. As EDG FOST SG increases (Ref. 3.10 & 3.21); the volume of the fuel oil required for EDG operation decreases. Review of this information indicates an uncorrected indicator
, elevation is equivalent in work (for low net heat value, Ref. 3.10) within 0.05% for any of the allowed SG readings (0.83 to 0.89), based upon:
[0.83 x Btu/LB(@0.83 SG)/Btu/Gai(@0.83 SG)]/[0.89 x Btu/LB(@0.89 SG)/Btu/Gal(@0.89 SG)] = 1 *-0.001
[0.83 x 18762 / 125987.6] / [0.8348 x 18736.9 / 126572.5] = 1.000 = 100.02%
[0.83 x 18762 / 125987.6] /[0.8448 x 18686.2 / 127754.5] = 1.000 = 100.03%
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 14 of 74
[0.83 x 18762 / 125987.6] [0.8550 x 18635.4 /128936.51 = 1.000 = 100.02%
[0.83 x 18762 / 125987.6] / [0.8654 x 18584.7 / 130118.5] = 1.000 = 100.04%
[0.83 x 18762 / 125987.6] / [0.8762 x 18523.8/131300.5] = 1.000 = 99.99%
[0.83 x 18762/ 125987.6] /[0.8871 x 18462.9 / 132581] = 1.001 = 100.05%
[0.83 x 18762 / 125987.6] / [0.890 x 18447.2 / 132884.4] = 1.000 = 100.04%
Corrected gallon value = (0.830/current SG) x Actual gallon required Magnetrol Switch This calculation uses fuel oil specific gravity (0.83 SG) for both the low-low and low magnetrol switch action. Any density changes resulting from the effects of temperature variations are included in the temperature effects (TE) for the Magnetrol level switches. Therefore, net adverse effect of PM on the Magnetrol Switches is negligible, (See Attachment 4.5 and Assumption 2.7).
At higher densities, both low-low and low magnetrol switch action would be slightly lower.
PMSG-LL = (1/8" / 0.1 [SG change]) x 0.06 [SG change] = 0.075" PMSG-L = (1" / 0.1 [SG change]) x 0.06 [SG change] = 0.6" Dipstick PM for sounding (internal 3" stilling pipe to within 2" of bottom) the tank is attributed to, process turbulence (if pump is running or tank is being filled) and or uncertainty in identification of wet to dry interface due to wicking on the dipstick. This PM value cannot be calculated, therefore, a value of +/-0.50" will be used in the evaluation. This value is considered conservative enough to include Readability error of approximately 1/4 of 1/16th of an inch or 0.0156".
- Uehlinq indicators Historically, the required fuel volume was calculated at a SG of 0.83 to maximize the required gallons value. The Uehling indicators are calibrated for a SG of 0.86. Density changes due to temperature increases or decreases will result in an increase/ decrease (respectively) in the actual tank level. However, the level indication, because it is based on head pressure, will remain almost unchanged and will therefore reflect the effective level relative to EDG run time. This is due to the increase in BTU/gallon (or Lbs of fuel/gallon). The effect of density changes due to temperature changes on the fuel available for EDG running time requirements are considered to be negligible.
For the required level indication, the actual gallon value is sufficient to provide the fuel inventory required to meet the EDG running time requirements, regardless of SG value. If the SG is less than 0.86, the uncorrected read elevation, and gallons, would be less than actual height and gallon value. If the SG is greater than 0.86, then the uncorrected read elevation, and gallons, is more than actual height and gallon value. If the SG >0.86, then the potential difference in SG from the calibrated 0.86 value will impact the total net heat value of unusable fuel oil below the switch actuation point, see sect. 7.2.1.2.
7.2.1.1 Uehling Indicators - Process impact for fuel oil SG (SGe)
The impact per +/-0.01 of SG changes is approximately 1.16% change in elevation reading (and resultant gallons), or a total of approximately +/-3.5% of reading for allowed SG span of 0.83 to 0.89.
PM for indicator includes readability.
SGO = 100 (0.87 - 0.85 / 0.86) = 2.32% for a 0.02 SG change at any specific value SGe = 2.32% / 2 = +/-1.16% for a +/-0.01 SG change (The SGe has linear impact on gallons)
Operators use graphs TC-25B or TC-25D to convert the indicated EDG tank level to gallons. The graphs identify the SG correction calculation to be used for a corrected tank level to achieve the +/-50 gallon accuracy identified in IP3-RPT-EDG-01 632.
Corrected inch value = (0.860/current SG) x Actual inch reading from LI
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 15 of 74 W 7.2.1.2 Indication SG error at low-low switch setpoint evaluation (SGie 1-1)
At the low-low switch setpoint (17.1") the process error is small, both for level and gallons required.
For a nominal setpoint (from Section 12.1) of 17.1 ", the LI is 20.17" (Low value for Tank 33, Tank 31 & 32 would be approximately 1" lower - See Table 1 for slope correction). From REF 3.12 the indicator does not measure level below 6" from the tank bottom. Therefore, measured head (mh)
@ LI:
mh = (20.17" - 6.0") = 14.17" (See Table 1)
SGe m= Indication Error = SGe x mh SGiel = + 1.16% x (0.03/0.01) x 14.17" = +/-0.492" [for -0.03 SGI The following is the potential impact on required indicated gallons due to SG >0.86 SGie 1-= +/-0.492" = +/-0.5" [rounded, max. SG1e-1 change, or +/-36, round to 40, gallons required]
7.2.1.3 Indication SG error at Low switch setpoint evaluation (SG, 8 1)
From REF 3.12 the indicator does not measure level below 6" from the tank bottom. For a nominal switch setpoint of 87.0" the LI is 89.27" for tank 31 & 32, 90.07" for tank 33 (See Table 1 for slope correction). Therefore, measured head @ LI (mh) = (90.07" - 6.0") = 84.07" SGi, ,= Indication Error = SG, x mh SGieI = Indication Error = +/- 1.16% x 84.07" = +/-0.975" [per +/-0.01 SG, +/-2.93" max. change
+/-0.03 SG]
. 7.2.1.4 Bounding indication SG error evaluation For bounding level at top of tank (108") @ LI (mh) = (108" - 6.0") = 102" Bounding Indication Error = +/- 1.16% x 102" = +/-1.18" [per +/-0.01 SG, +/-3.5" max. change :0.03 SG]
Therefore, indication could be 3.5" lower than actual when the tank is full of fuel oil @ 0.83 SG, or 3.5" higher than actual when the tank is full of fuel oil @ 0.89 SG.
7.2.2 Other Dipstick Uncertainties (Indicator Readability)
Readability effect (Approximately 1/4 of 1/16th of an inch, the smallest marking) for the Dipstick is included in the PM value (See Section 7.2.1).
7.2.3 Uehling Indicator PM for indicator readability, for use in this Calculation Readability effect for the manometer (Approximately 1/4 of 1/4 of an inch) is included in the PM value for the Uehling indicators (See Section 8.1.8). For conservatism a value of 1.25 x RA will be used to envelope readability error of .0625" and any unidentified PM uncertainties (pump running turbulence, etc.).
RA = level at the indicator +/- 1/8" (see Section 8.1.1)
PM = +/- 0.16" 8.0 MODULE UNCERTAINTY 8.1 Level Switch (LC-1 204S, LC-1205S & LC-1206S) -Magnetrol model A-1 53-FTDM (Reference 3.19
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 16 of 74
& See Attachment 4.2) (el) for LOW-LOW level (17.1" pump protection level) & (e 2) for LOW level (87" or 87.5" for low level alarm)
Level Indicator, Dipstick (e 3)
Level Indicator (LI-1 133, L-1 134 & LI-1 135) -Uehling model 55R1 73 (tank 31 & 32 @ 87.5" level -
e4), (tank 33 @ 87" level - e5), (tank 31 & 32 @ 17.1u level - e 6) & (tank 33 @ 17.1" level - e7) 8.1.1 Reference Accuracy (RA)
- Magnetrol Switch Magnetrol specifies an accuracy of +/-1/4" for the actuation diaphragm and switch (See attachment 4.4)
- Digstick Based on Engineering Judgment, an accuracy value of +/-1/16" is applied for this device (the smallest marking).
- Uehlinq indicators Uehling specifies an accuracy of +/-1/8" of level measurement (See attachment 4.13)
. 8.1.2 Drift(DR)
Past performance Data is not available and vendors do not provide a drift factor for these devices.
Based on Engineering Judgment, for devices of this type, it is assumed that drift is accounted for in (RA). Therefore, a value of 0.0 will be used for DR in this evaluation.
8.1.3 Temperature Effect (TE)
- Maqnetrol Each EDG FOST tank is located underground, with the switch housing flange approx. 38" above the tank cylinder. The temperature of the fuel oil (density, viscosity) affects the displacer point of action. Normal environment of the EDG underground FOST tank location is 35 0 F - 11 0°F [use 70°F +/-40°F] (See Attachment 4.2).
The Magnetrol installation drawings show the switch settings at temperature from 1000 to 3000 F. Compensation to 30°F is by extrapolating the 1000 and 2000 values. Values are approximately 0.5" per 100°F.
TE = +/- (40 0 F) X 0.5"/1000 F (See Assumption 2.1)
TE =0.2"
- Dipstick For the Dipstick indicator the TE is not applicable
- Uehlinq For the Uehling indicators the TE is not applicable (See attachment 4.13)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 17 of 74 8.1.4 Measurement and Test Equipment uncertainty (MTE) 0 Magnetrol switches MTEI: Tape measure (or Dipstick), accuracy +/-1/16" MTE 2 : When taking measurements, an error due to flex in the tape measure or flex in the cable can occur. Therefore, an error of +/-1/2" is a conservative estimate. Due to this conservative estimate indicator Readability is not evaluated as a separate uncertainty.
2 MTE = * (MTE 1 + MTE2 1/2 MTE +/- (0.06252 + 0.5 ) /2' MTE = +/- 0.5"
° Dipstick MTE for the dipstick is not applicable
- Uehling Indicators Calibration is not required; therefore, MTE for the Uehling indicators is not applicable (See attachment 4.13) 8.1.5 As-Left Tolerance = (ALT) NOTE: ALT is equal to Calibration Tolerance (CT).
- Maunetrol switches The As-Left Tolerance is the technician precision in setting the tolerance of a device during installation or verification. The instrument surveillance procedure for these switches does not presently require measuring or resetting of the displacers.
Since no specific instrument calibration procedure is approved for LC-1 204S, LC-1 205S or LC-1 206S, the As-Left tolerance will be evaluated based on Assumption 2.5.
ALT = +/-2.4 x (0.25")
ALT = +/-0.60"
- Dipstick ALT for the Dipstick is not applicable Uehlincq indicators Calibration is not required; therefore, ALT/CT for the Uehling indicators is not applicable (See attachment 4.13) 8.2 Magnetrol Level Switch Uncertainty (el) & (e 2), and As-Found Tolerance (AFT) 8.2.1 LOW-LOW Level Switch (Lower Displacer) uncertainty (el) 2 2 2 el= (RA 2 + DR 2 + TE + MTE + ALT 2)"
el +/- (0.252 + 0.02 + 0.202+ 0.502 + 0.602)112 e= +/- 0.84"
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 18 of 74 8.2.2 LOW Level Switch (Upper Displacer) uncertainty (e 2)
The value of e 2 is based on the uncertainty associated with the LOW-LOW Level displacer, which is similar to the LOW Level Displacer, therefore e 2 is the same as the el value.
e2 +/- (e e 2 =t (0.842)1/2 e 2 = +/- 0.84" The LOW-LOW Level setting & LOW Level setting relationship has impact on the fuel oil inventory between the two displacer settings. Since the low-low and low switch As-Found values, with uncertainty are used for evaluating available fuel oil, there is no need to separately evaluate the uncertainty of the difference between the values.
8.2.3 As-Found Tolerance (AFT) for the Magnetrol Switches As-Found Tolerance2 (AFT) for the Magnetrol Switches will be determined by:
AFT = +/- (RA 2 + DR +ALT 2)12 AFT = +/- (0.252 + 0.02 +0.602)1/2 AFT = +/- 0.65" 8.3 Level Indicator (dipstick direct reading) Uncertainty (e 3).
The dip stick direct reading uncertainty only includes RA (see 8.1.1) e 3 = +/- (RA 2)112 = +/- (0.06252)/2 e 3 = +/- 0.0625" 8.4 Level Indicator Uncertainty - Manometer/Bubbler Reading (e 4 / e5 / e6 / e7 )
The dip stick direct reading uncertainty only includes RA (see 8.1.1) e 5 = e 4 = e 6 e 7 = +/- (RA) = (0.1252)1/2 e5 = e 4 = e 6 = e7 = +/- 0.125" 9.0 CALCULATE CHANNEL UNCERTAINTY 9.1 Maqnetrol Switch (LS) 9.1.1 FOR LOW-LOW SWITCH SETTING (CU1 ):
CU1 = +/- (PMSG-ýL 2 + PE 2 + e 12 + IRE2)"1 2 +/-B" CU, = +/- (0.0752+ 02+ 0.842+ 02)112 +/-0" (see Section 7.2.1 & 8.2.1)
CU, = +/- 0.84" 9.1.2 FOR LOW SWITCH SETTING (CU 2):
CU2 = +/- (PMsYG-L2 + PE2+ e 220+ IRE 2 ) 1/2 +/-B" CU 2 = +/- (0.6 0.842 + s0" (see Section 7.2.1 & 8.2.2)
CU 2 = +/- 1.03"
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 19 of 74 9.2 UehlinQ Indicator - Manometer/Bubbler Reading 9.2.1 Evaluate CU4 ICUdCUW/CU 7 - For Tank 31, 32 & 33 9.2.1.1 FOR LI AT LOW LS SETTING: (CUSCUs) - [without correction for SG]
e 4 = e 5 = level at the indicator +/- 1/8" (see Section 8.1.1)
PM = +/- RA x 1.25 PM = +/- 0.125" x 1.25 = 0.15625" - Round to 0.16" PM =+/- 0.16" CU 4 = CUs = +/- (e42 + PM2 ) 112 = +/- (0.1252 + 0.162)1/2= +/- 0.2" CU 4 = CU 5 = +/- 0.2" 9.2.1.2 FOR LI AT LOW-LOW LS SETTING: (CU&'CU 7 ) - [without correction for SG]
e6 = e7 = level at the indicator +/- 1/8" (see Section 8.1.1)
PM = +/- RA x 1.25 PM = +/- 0.125" x 1.25 = 0.15625" - Round to 0.16" PM = +/- 0.16" CU6 = CU 7 = +/- (e42 + PM 2) 112 = +/- (0.1252 + 0.162)1/2= +/- 0.2" CU8 = CU 7 = +/- 0.2" 9.2.2 Evaluate CU 4 ICUd/CUgCU 7 - For Tank 31, 32 & 33 -[corrected for SG]
9.2.2.1 Evaluate CU 4 (tank 31 & 32) & CU5 (tank 33) (@ TS LOW Setpoint)
CU4 and CU5 have essentially the same considerations at 6804 gallon (87" & 87.5") alarm value -
e4 = e5 level at the indicator +/- 1/8" (see Section 8.1.1)
PM =+/- 0.16" 2 2 2 CU 4 = CU 5 = +/- (e42 + pM + SGie 1 )11 CU4 CU 5 = +/- (0.1252 + 0.162+ 2.932)1/2 = +/- 2.94" - Round to 2.95" CU 4 = CU 5 = +/- 2.95" 9.2.2.2 Evaluate CU 6 (tank 31 & 32) & CU 7 (tank 33) (@ TS LOW-LOW Setpoint)
CU 6 and CU 7 have essentially the same considerations at 17.1" pump shut off value -
RA = level at the indicator +/- 1/8" (see Section 8.1.1) e 6 = e7 = level at the indicator +/- 1/8" (see Section 8.1.1)
PM =+ 0.16" CU 6 = CU 7 = +/- (RA + PM + SGie 1.-2)1/2 2 2 CU 6 = CU 7 +/- (0.1252 + 0.162+ 0.52)1/2 +/- 0.5397" - Round to 0.55" CU6 = CU 7 = +/- 0.55" 9.3 FOR DIPSTICK LEVEL INDICATION (TANK SOUNDING)
The dip stick (direct reading) uncertainty includes e 3 (see 8.3) & PM (see 7.2.1).
CU 3 = +/- (e 32 + PM 2 )"2 +/- (0.06252 + 0.50)
CU3 = +/- 0.5" [This reading is uncorrected for any SG effects)
CU 3 = +/- 0.5" (see section 8.3)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 20 of 74 10.0 EDG TANKS 10.1 EVALUATE ERROR DUE TO TANK SLOPE FOR TABLE 1 - [Ref. Att 4.12 - IP3-RPT-EDG-01632]
10.1.1 EVALUATE ERROR DUE TO SLOPE OF TANK NO. 31 AND NO. 32 The change in height over horizontal 51.0" is 1.0625" (See Attachment 4.12)
TAN p = 1.0625" = 0.0208333 51.0" (p= 1.19350 (tank tilt in degrees)
Determine AH Between The Tank Centerline and The Pump Location The distance between the centerline and the pump is 61.0" (Ref. 3.7.2)
AH = TAN Px 61.0" = .'. 0.0208333 x 61.0" = 1.2708"
.,. For any height at the tank centerline (H), the height at the pump will be H-1.2708" (INPUT FOR TABLE 1)
Determine AH Between The Tank Centerline and The Level Switch Location The distance between the centerline and the level switch is 79.0" (Ref. 3.7.2)
AH = TAN px 79.0" = .-. 0.0208333 x 79.0 = 1.6458"
.*.For any height at the tank centerline (H), the height at the level switch is H-1.6458" (INPUT FOR TABLE 1)
Determine AH Between The Tank Centerline and The Level Indicator Location The distance between the centerline and the level indicator is 30.0" (Ref. 3.7.2)
AH = TAN px 30.0" = .'. 0.0208333 x 30.0 = 0.6249"
.,. For any height at the tank centerline (H), the height at the level indicator is H+ 0.6249" (INPUT FOR TABLE 1)
Determine AH Between The Tank Centerline and The Soundinq Tube Location The distance between the centerline and the Sounding Tube is 81.0" (Ref. 3.7.2)
AH = TAN px 81.0" = .'. 0.0208333 x 81.0 = 1.6875"
.-. For any height at the tank centerline (H), the height at the sounding tube is H+ 1.6875" (INPUT FOR TABLE 1)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 21 of 74
. 10.1.2 EVALUATE ERROR DUE TO SLOPE OF TANK NO. 33 The change in height over 51.0" is 1.4375" (See Attachment 4.12)
TAN ip = 1.4375" = 0.0281863 51.0"
.' = 1.61450 (tank tilt in degrees)
Determine AH Between The Tank Centerline and The Pump Location The distance between the centerline and the pump is 61.0" (Ref. 3.7.2)
AH =TAN q)x 61.0" = .'. 0.0281863 x 61.0" = 1.7194"
.*.For any height at the tank centerline (H), the height at the pump will be H-1.7194" (INPUT FOR TABLE 1)
Determine AH Between The Tank Centerline and The Level Switch Location The distance between the centerline and the level switch is 79.0" (Ref. 3.7.2)
AH = TAN (px 79.0" = .'. 0.0281863 x 79.0 = 2.2267"
,. For any height at the tank centerline (H), the height at the level indicator is H-2.2267"
- (INPUT FOR TABLE 1)
Determine AH Between The Tank Centerline and The Level Indicator Location The distance between the centerline and the level indicator is 30.0" (Ref. 3.7.2)
AH = TAN 9 x 30.0" = .'. 0.0281863 x 30.0 = 0.8456"
.*.For any height at the tank centerline (H), the height at the level switch is H+ 0.8456" (INPUT FOR TABLE 1)
Determine AH Between The Tank Centerline and The Sounding Tube Location The distance between the centerline and the sounding tube is 81.0" (Ref. 3.7.2)
AH = TAN p x 81.0" = .-. 0.0281863 x 81.0 = 2.2831"
.,. For any height at the tank centerline (H), the height at the sounding tube is H+ 2.2831" (INPUT FOR TABLE 1)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 22 of 74 10.2 DETERMINE EDG FUEL REQUIREMENT Technical Specification Task Force Change Traveler TSTF-501 A identifies allowed standard format changes to Technical Specifications to identify need for 7 days of EDG fuel oil storage, and AOT if only 6 days of EDG fuel oil storage is maintained. The 6 day and 7 day terms replace actual gallon values to minimize future Technical Specification changes and allow the 50.59 controlled site procedures and programs to control and justify the required volumes.
Fuel is to be stored in site tanks for operation of each EDG for total of either 6 or 7 days (144 or 168 hours0.00194 days <br />0.0467 hours <br />2.777778e-4 weeks <br />6.3924e-5 months <br />) at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile. Site tanks are defined as the local EDG FOST and other site tanks, which are maintained to the same fuel oil standards, and would contain the EDG oil until transferred to the EDG FOST. Existing 1P3 Technical Specification required volume for each EDG is 5365 gallons, based upon minimum safeguards loading for 48 hours5.555556e-4 days <br />0.0133 hours <br />7.936508e-5 weeks <br />1.8264e-5 months <br />. Prior EDG fuel oil calculations identified 5871 gallons required to operate the EDG at nameplate loading for 48 hours5.555556e-4 days <br />0.0133 hours <br />7.936508e-5 weeks <br />1.8264e-5 months <br />. After review of the required volumes, size of the EDG FOST, and the fuel oil used during EDG required testing, it was decided that fuel oil for 40 hours4.62963e-4 days <br />0.0111 hours <br />6.613757e-5 weeks <br />1.522e-5 months <br /> of EDG operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile would provide adequate fuel oil while allowing for required testing without requiring unreasonable frequency of EDG FOST refill.
From reference 3.10, we have the following information regarding fuel oil required for each EDG:
[24 hour maximum profile is Y2 hour @ 2000KW, 2 hour2.314815e-5 days <br />5.555556e-4 hours <br />3.306878e-6 weeks <br />7.61e-7 months <br /> @ 1950KW & 2112 hour0.0244 days <br />0.587 hours <br />0.00349 weeks <br />8.03616e-4 months <br /> @ 1750KW]
a 23,940 gallons, @ SG of 0.83, for 7 day (168 hour0.00194 days <br />0.0467 hours <br />2.777778e-4 weeks <br />6.3924e-5 months <br />) operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile
- 20,520 gallons, @ SG of 0.83, for 6 day (144 hour0.00167 days <br />0.04 hours <br />2.380952e-4 weeks <br />5.4792e-5 months <br />) operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile
- 6,840 gallons, @ SG of 0.83, for 48 hour5.555556e-4 days <br />0.0133 hours <br />7.936508e-5 weeks <br />1.8264e-5 months <br /> operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile
- 141 gallons/hr, @ SG of 0.83, at 100% (1750KW) EDG loading The required number of gallons to run the EDG for a specified time varies based upon the actual SG of the fuel oil to be used, based upon the mass and volumetric low (net) heat available. The relationship may be approximated by the following formula:
[Gallons @ 0.83 SG] x 0.83 / [actual SG] = Gallons @ actual SG 6,840 gallons & 141 gal/hr at 0.83 SG is equivalent to:
6,601 gallons & 136 gal/hr at 0.86 SG or 6,376 gallons & 131.5 gal/hr at 0.89 SG 10.2.1 Required fuel oil for 40 hours4.62963e-4 days <br />0.0111 hours <br />6.613757e-5 weeks <br />1.522e-5 months <br /> operation of an EDG [part of 144 and/or 168 hour0.00194 days <br />0.0467 hours <br />2.777778e-4 weeks <br />6.3924e-5 months <br /> requirement]
Fuel oil for 40 hours4.62963e-4 days <br />0.0111 hours <br />6.613757e-5 weeks <br />1.522e-5 months <br /> of EDG operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile is stored in each EDG FOST:
6,840 gallons - (8 x 141 gallons) = 6,840 - 1128 = 5,712 gallons @ SG 0.83 6,601 gallons - (8 x 136 gallons) = 6,601 - 1088 = 5,513 gallons @ SG 0.86 Less than 5,712 gallons @ 0.83 SG [or equivalent] will cause entry into associated FSAR/TRM AOT 10.2.2 Required fuel oil be stored in tanks other than the EDG FOST - for an additional 128 hours0.00148 days <br />0.0356 hours <br />2.116402e-4 weeks <br />4.8704e-5 months <br /> operation of an EDG [part of 144 hour0.00167 days <br />0.04 hours <br />2.380952e-4 weeks <br />5.4792e-5 months <br /> (6 day) and/or 168 hour0.00194 days <br />0.0467 hours <br />2.777778e-4 weeks <br />6.3924e-5 months <br /> (7 day) requirement]
Fuel for 128 hours0.00148 days <br />0.0356 hours <br />2.116402e-4 weeks <br />4.8704e-5 months <br /> (168-40) of EDG operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile stored in other site tanks:
23,940 gallons - 5,712 gallons = 18,228 gallons @ SG 0.83 for each EDG Less than 18,228 usable gallons @ 0.83 SG [or equivalent] for any EDG will cause entry into associated FSAR/TRM AOT and needs to be evaluated for impact on Technical Specification Requirements. A minimum of 36,456 gallons (2x 18,228, for two IP3 EDG operable), and a minimum of 54,684 gallons (3x 18,228, for three IP3 EDG operable), is required to be stored in tanks other than the EDG FOST.
Reduction below the 7-Day required amount, by up to 3,420 gallons @ SG 0.83 results in 6-Day AOT entry for the specified EDG. 6840 (for 48 hours5.555556e-4 days <br />0.0133 hours <br />7.936508e-5 weeks <br />1.8264e-5 months <br />)/2 = 3420 (for 24 hours2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br />)
GT2/GT3 Fuel Oil Tank volume is 583 gallons/inch, and is equipped with a Varec 2500 ATG measuring tape (accurate to +/-0.5"). The required IP3 gallons should include an additional 1,000 gallon allowance for reading accuracy, and a minimum log reading of 55,684 gallons for 3 EDG operable (NO AOT).
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 23 of 74 10.3 EDG F.O. Day Tank Considerations There are 3 EDG (Emergency Diesel Generator) Fuel Oil (FO) 175 gallon Day Tanks, one for each EDG. The EDG Fuel Oil Day Tank has level switches which actuate when the tank level is at specific levels, Level Switches (LC-1207S, LC-1208S & LC-1209S):
0 90% [Fill valve opens on decreasing level or closes on increasing level],
- 65% (EDG FO storage tank transfer pump start (auto stop between 65% & 90% rising level)] and 0 50%/30% [EDG day tank low level alarm, see CR-IP3-2011-05558 for conflicting information]
Evaluate the EDG Fuel Oil Day Tank volumes at 65% and 50%/30% to identify the time EDO may operate at EDO 100% Load (1750 KW) before day tank empties, with no EDO FOST transfer pump makeup.
EDG Fuel Oil Day Tank volume: 65% x 175 gallon = 113.75 gallons EDG Full Load fuel usage: 141 gallons/hr, @ SO of 0.83 [Reference 3.10]
.-.Therefore: 113.75 gals x 60 min /hr = 48.4 minutes to tank empty 141 gallons/hr EDG Fuel Oil Day Tank volume: 50% x 175 gallon = 87.5 gallons EDG Full Load fuel usage: 141 gallons/hr, @ SG of 0.83 Therefore: 87.5 -als x 60 min /hr = 37.2 minutes to tank empty 141 gallons/hr EDG Fuel Oil Day Tank volume: 30% x 175 gallon = 52.5 gallons EDO Full Load fuel usage: 141 gallons/hr, @ SG of 0.83 Therefore: 52.5 gals x 60 min /hr = 22.3 minutes to tank empty 141 gallons/hr
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 24 of 74
. 11.0 ANALYTICAL LIMIT (AL)
No AL is established in theOR NOMINAL FSAR PROCESS or Technical LIMIT (NPL)
Specifications.
The IPEC underground FOST was not designed to hold seven days' worth of ultra low sulfur fuel oil with the EDG operating at its maximum load profile conditions. Thus, the strategy has always been that to meet the seven day EDG run stipulation of Regulatory Guide 1.137, the FOST would be provided with fuel oil on an as needed basis from an on site reserve supply. Because of this strategy with respect to the necessity of re-filling the FOST, in addition to the seven day time, IPEC also contains in its current licensing basis a 48 hour5.555556e-4 days <br />0.0133 hours <br />7.936508e-5 weeks <br />1.8264e-5 months <br /> EDG operating time period specifically related to the initial FOST fuel oil usable volume. It is not cited in nor is it a requirement of Regulatory Guide 1.137.
This IPEC specific interim time period must also be addressed by the License Amendment Request (LAR) process. FOST fuel oil usable and stored volumes, and the corresponding EDG run time, will change. The newly determined FOST volumes and associated EDG run time will not be put in the Technical Specifications but will be placed in the Technical Specification Bases or the FSAR/TRM.
This calculation is to support a planned Technical Specification Amendment request associated with EDG FO volumes in accordance with TSTF-501A. Technical Specifications would identify the need for 7 days and/or 6 days worth of fuel, to be stored in each EDG FOST and other on-site tanks. There is then a need to place a specific EDG FOST volume requirement in a 50.59 controlled document, such as the FSAR/TRM or Technical Specification Basis. Reference 3.10 indicates the EDG FOST is not large enough to store 48 hours5.555556e-4 days <br />0.0133 hours <br />7.936508e-5 weeks <br />1.8264e-5 months <br /> worth of useable fuel [past Technical Specification requirement],
so the basis for a new volume will be established in this calculation.
O 11.1 PROCESS LIMIT (NPL) FOR EDG FOST (FSAR/TRM):
Considerations -
Maximum volume in any EDG FOST is 7650 gallons to prevent flooding of the local indicators, per 3-SOP-EL-009.
Unusable fuel gallons based upon allowed as-found for pump shut-off switch (section 13.1).
5712 usable gallons of fuel oil for 40 hours4.62963e-4 days <br />0.0111 hours <br />6.613757e-5 weeks <br />1.522e-5 months <br /> operation of EDG operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> rating (section 10.2.1).
Additional fuel volume in each EDG FOST to account for periodic testing of each EDG will be based on approximately six hours of full load testing operation (TS SR 3.8.1.2 & 3.8.1.3 or return to service testing):
141 gal/hr [100%, 1750KW] x 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> = 846 gallons @ 0.83 SG Therefore, FSAR/TRM Process Limit will be 5712 [@ 0.83 SG] useable gallons of fuel oil (or 5513 gallons
@ 0.86 SG) to be stored in each EDG FOST, which would provide for 40 hours4.62963e-4 days <br />0.0111 hours <br />6.613757e-5 weeks <br />1.522e-5 months <br /> of EDG operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile load and 18,228 useable gallons of fuel oil for 128 hours0.00148 days <br />0.0356 hours <br />2.116402e-4 weeks <br />4.8704e-5 months <br /> of EDG operation at 24 hour2.777778e-4 days <br />0.00667 hours <br />3.968254e-5 weeks <br />9.132e-6 months <br /> maximum profile to be stored in other site tanks (Sect. 10.2.1).
11.1.1 NPL for FSAR/TRM value for EDG FOST usable gallons - Dipstick Tank 33 Tank 31 & 32 Using Dipstick 5712 5712 Useable gallons [40 hours @ SG of 0.83] (Sect. 10.2.1) 956 915
- Unusable gallons [Difference due to tank tilt] (Sect. 13.1) 20 20 Coating of tank - margin (Ref. 3.2 & 2.14) 6688 6647 Total gallons @ SG 0.83
- Tank unusable gallons are based upon the allowed As-Found value for pump shut-off switch.
For Tank 31 & 32 NPL = 5712 usable gals, 6647 gals in the tank (See Table 1)
NPL = 87.69898 @ the sounding tube (round to 87.7")
NPL = 87.7" For Tank 31 & 32
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 25 of 74 For Tank 33 NPL = 5712 usable gals, 6688 gals in the tank (See Table 1)
NPL = 88.87515" @ the sounding tube (round to 88.88")
NPL = 88.88" For Tank 33 11.1.2 NPL for FSAR/TRM value for EDG FOST usable gallons - Indicator Tank 33 Tank 31 & 32 Using Uehlnna Indicators [Calibrated at 0.86 SGI 5513 5513 Useable gallons [40 hours @ SG of 0.86] (Sect. 10.2.1) 956 915
- Unusable gallons [Difference due to tank tilt] (Sect. 13.1) 20 20 Coating of tank - margin (Ref. 3.2) 40 40 Margin & Specific Gravity (SG) - (Sect 7.2.1.2) 50 50 Indication accuracy (Ref. 8.4.1) 6579 6538 Total gallons @ SG 0.86 Tank unusable gallons are based upon the allowed As-Found value for pump shut-off switch.
For Tank 31 & 32 -
NPL = 5513 usable gals, 6538 gallons by indicator in the tank, @ SG 0.86 (See Table 1)
NPL = 85.16" on the Indicator (round up to 85.2") [86.2" @ SG 0.86 at the sounding tube]
NPL = 85.2" on the Indicator - For Tank 31 & 32 For Tank 33 -
NPL = 5513 usable gals, 6579 gallons by indicator in the tank, @ SG 0.86 (See Table 1)
NPL = 85.93" on the Indicator (round up to 85.95") [86.8" @ SG 0.86 at the sounding tube]
NPL = 85.95" on the Indicator - For Tank 33 11.2 NOMINAL PROCESS LIMIT (NPL) FOR LOW-LOW LEVEL DISPLACER SETTING LIMIT:
To protect the fuel oil transfer pumps from the damaging effects of vortexing, the IP3 FSAR and the manufacturer pump submergence data indicates a low level pump cut-off of 12" (See Attachment 4.3).
This protection contributes unusable gallons in the tanks, and is different due to tank slope (0.50" for tank 33 and 0.375" for tank 31 & 32) from the switch down to the pump.
From the Rockaway Tank drawing and the Gould Pumps outline drawings; the pump suction is 3,875" above the tank bottom as shown below (Reference 3.7 (2) & (3)).
108 (O---) + 78 - 129.75 + 2 - 0.375 = 3.875" The tolerance on all pump dimensions is +1/8" or +1/8" per 5', which ever is greater. The total dimensional error applied will be +3/8". (ref, 3.7 (3))
Therefore, for pump protection the NPL will be based on the manufacturer's submergence value plus distance from tank bottom plus the dimensional error.
NPL = 12" + 3.875" + 0.375" = 16.25" For Tank 31 & 32 NPL = 16.250" @ the pumps [15.875 @ the switch],
NPL = 788 gals in the tank (See Table 1)
For Tank 33 NPL = 16.250" @ the pumps [15.7427 @ the switch],
NPL = 818 gals in the tank (See Table 1)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 26 of 74 NOMINAL PROCESS LIMIT (NPL) REVISED LOW LEVEL DISPLACER SETTING LIMIT:
. 11.3 Maximum level in any EDG FOST is 7650 gallons to prevent flooding of the local indicators, per 3-SOP-EL-009 Fuel volume required to account for periodic testing of each EDG will be based on approximately six hours of full load operation per TS SR 3.8.1.2 & 3.8.1.3 or return to service testing:
141 gal/hr [full load operation] x 6 hours6.944444e-5 days <br />0.00167 hours <br />9.920635e-6 weeks <br />2.283e-6 months <br /> = 846 gallons @0.83 SG NPL for alarm to be based on maximum level minus the fuel allowance for testing is:
7650 - 846 = 6804 gallons @0.83 SG 11.3.1 Nominal process limit (NPL) - Low Level Alarm value to protect FSAR/TRM value By design, an alarm will be actuated when there is 6804 gallons of fuel in any EDG FOST. (Ref 3.13)
For Tank 31 & 32 NPL = 86.58466" @ the switch NPL = 6804 gals in the tank (See Table 1).
NPL = 86.585" (round to 86.6") - For Tank 31 & 32 NPL = 86.6" For Tank 33 NPL = 86.00376" @ the switch NPL = 6804 gals in the tank (See Table 1)
NPL = 86.004" (round to 86.0") - For Tank 33 NPL = 86.0"
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 27 of 74 12.0 DETERMINE SETPOINT (TS)
TS = NPL +/- (CU + Margin)
Positive values of CU is used for process variables that decrease towards the analytical limit.
12.1 LOW-LOW LEVEL DISPLACER SETPOINT SETTING:
Nominal TS of 17.1" @ the switch was implemented for tanks 31, 32, & 33 in 1994 12.1.1 Lower Displacer Setting for pump protection - For Tank 31 & 32 TS = NPL + CU - For Tank 31 & 32 TS = 15.875" + 0.84" (See Section 11.2 and 9.1.1)
TS = 16.715" @ the switch = 844 gals - Calculated setting (round to 16.7")
Implemented - For Tank 31 & 32 (see TABLE 1)
TS = 17.1" @ the switch = 870 gallons Existing implemented setting is conservative.
12.1.2 Lower Displacer Setting for pump protection - For Tank 33 TS = NPL + CU - For Tank 33 TS = 15.7427" + 0.84" (See Section 11.2 and 9.1.1)
TS = 16.5827" @ the switch = 875 gals - Calculated setting (round to 16.6")
Implemented - For Tank 33 (see TABLE 1)
TS = 17.1" @ the switch = 910 gallons Existing implemented setting is conservative.
12.1.3 Lower Displacer Setting - LOW-LOW switch field setting, TS =17.1" (see Section 12.1)
Level switch displacer calibrations referenced from tank bottom to bottom of displacer. From the Magnetrol installation drawing (Att. 4.2), the lower switch transfers on decreasing level of at least 1.125" (1 1/8") above the bottom of the lower displacer. Therefore the bottom of the lower displacer will be the setpoint (TSLow.Low) minus 1.125":
LOW-LOW field setting = 17.1" - 1.125" = 15.975" From the Tank Bottom to the Bottom of the Displacer (TBBD) 12.2 LOW LEVEL DISPLACER SETPOINT SETlING:
This evaluation for the Upper Displacer Setting Limit will consider 6804 gallon alarm identified in Section 11.3.
12.2.1 Upper Displacer Setting for low level 6804 gallon alarm setting - For Tank 31 & 32 TS = NPL + CULow TS = 86.585" + 1.03" (See Section 11.3.1 and 9.1.2)
TS = 87,615" @ the Switch, Rounded to 87.6" For Tank 31 & 32 (see TABLE 1) 6874 gallons TS = 87.6" @ the Switch = 6874 gals = 89.9" @ indicator = 90.95" @ sounding tube (See TABLE 1)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 28 of 74 12.2.2 Upper Displacer Setting for low level 6804 gallon alarm setting - For Tank 33 TS = NPL + CULOW TS = 86.004" + 1.03" (See Section 11.2.2 and 9.1.2)
TS = 87.034" @ the Switch, Rounded to 87.05" For Tanks 33 (see TABLE 1) 6874 gallons TS = 87.05" @ the Switch = 6874 gals = 90.1" @ indicator = 91.55" @ sounding tube (See TABLE 1) 12.2.3 Upper Displacer Setting - LOW Level switch field setting (see Section 12.2)
Level switch displacer field settings are referenced from tank bottom to bottom of displacer. From the Magnetrol installation drawing (Ant. 4.2), the upper switch transfers on decreasing level 3.5" (3 1/2")
above the bottom of the upper displacer. Therefore, the upper displacer will be set at the setpoint (TSLO) minus 3.5":
Tank 31 & 32 -
For field setting based on 6804 gallons in the tank, TS =87.6" (see Section 12.2.1)
LOW setting = 87.6" - 3.5" = 84.1" From the Tank Bottom to the Bottom of the Displacer (TBBD)
Tank 33 -
For field setting based on 6804 gallons in the tank, TS =87" (see Section 12.2.2)
LOW setting = 87.05" - 3.5" = 83.55" From the Tank Bottom to the Bottom of the Displacer (TBBD)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 29 of 74 12.3 TANK LEVEL- FSARrIRM MINIMUM LOW LEVEL INDICATION:
12.3.1 MINIMUM LEVEL INDICATION - Dipstick The EDG FOST minimum Dipstick indication required volume is 6647 gallons, @ 0.83 SG, for tank 31
& 32 volume and 6688 gallons, @ 0.83 SG, for tank 33 volume (see section 11.1.1), using the dipstick
@ the sounding tube.
From TABLE 1 this minimum volume is equivalent to 87.7" for Tank 31 & 32 and 88.88" for Tank 33.
The dipstick channel uncertainty (CU) associated with using the dipstick @ the sounding tube is
+/-0.50". The CU will be added to 87.7" for Tank 31 & 32 and to 88.88" for Tank 33; to determine the minimum read setting (TS) for the fuel oil to be measured in the tanks in Operations procedures.
TS for Tank 31 & 32 TS = 87.7" + CU TS = 87.7" + 0.50" = 88.2" TS = 88.2" = 6682 gallons (See TABLE 1) - @ 0.83 SG TS for Tank 33 TS = 88.88" + CU TS = 88.88" + 0.50" = 89.38" (Round up to 89.4")
TS = 89.4" = 6726 gallons (See TABLE 1) - @ 0.83 SG 12.3.1 MINIMUM LOW LEVEL INDICATION - Indicator The EDG FOST minimum Indicator required volume is 6538 gallons, @ 0.86 SG, for tank 31 & 32 volume and 6579 gallons, @ 0.86 SG, for tank 33 volume (see section 11.1.2) when the tank level indicators are used to obtain level. From TABLE 1 this volume is equivalent to 85.2" at the Level Indicators for Tank 31 & 32 and 85.95" at the Level Indicator for Tank 33.
The tables (see section 11.1.2) identifying these values already include specific allowances for indicator uncertainty and SG affects, therefore additional allowances would not be appropriate.
TS for Tank 31'& 32 Indication TS = 85.2" @ the Indicator = 6538 gallons @ SG 0.86 TS for Tank 33 indication TS = 85.95" @ the Indicator = 6579 gallons @ SG 0.86
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 30 of 74 13.0 DETERMINE AS FOUND VALUE (AFV) 13.1 LOW-LOW LEVEL DISPLACER AS FOUND VALUES:
The SRSS of RA, DR and ALT will be subtracted from the pump cut-off setpoint (TS) to determine the minimum As-Found Value for the pump cutoff switch level setting. The SRSS of RA, DR and ALT will be added to the pump TS for inventory control maximum As-Found Value.
2 21 2 AFVL-L = TS +/- (RA + DR + ALT ) /
2 AFVL.L = 17.1" +/- (0.252 + 0 + 0.60t)112 AFVL.L = 17.1" +/- 0.65" AFVL-L L= 16.45" (Lower AV for Pump Protection)
AFVL.L H= 17.75" (Upper AV for Inventory Control)
For Tank 31 & 32 (see TABLE 1)
AFVL.L L= 826 gals AFVL.L H= 915 gals For Tank 33 (see TABLE 1)
AFVL.L L= 866 gals AFVL.L H = 956 gals 13.2 LOW LEVEL DISPLACER AS FOUND VALUE:
TS elevation was determined in Section 12.2. To determine the minimum As Found Value for fuel oil 6804 gallon alarm setting; the SRSS of RA, DR and ALT for the switch will be subtracted from the Low Level Alarm calculated trip setpoint (TS). To determine the maximum As Found alarm value, the SASS of RA, DR and ALT for the switch will be added to the the Low Level Alarm calculated trip setpoint (TS), for impact on tank fill.
13.2.1 As Found Value for Low Setpoint Setting at 6804 gallon alarm setting - For Tank 31 & 32 (see TABLE 1) 2 2 12 AFVL = TS +/- (RA +DR + ALT ) 1 2
AFVL = 87.55" +/- (0.252 + 0 + 0.602)1/2 AFVL = 87.55" +/- 0.65" AFVL L= 86.9" (Lower AV for Inventory Control)
AFVL H = 88.2" (Upper AV for tank fill)
AFVL-L = 6827 gals (Lower AV for Inventory Control)
AFVL H = 6914 gals (Upper AV for tank fill) 13.2.2 As Found Value for Low Setpoint Setting at 6804 gallon alarm setting - For Tank 33 (see TABLE 1) 2 2 21 AFVL = TS t (RA +DR + ALT ) /2 AFVL = 87.05" +/- (0.252 + 0 + 0.602)112 AFVL = 87.05" +/- 0.65" AFVL L= 86.4" (Lower AV for Inventory Control)
AFVL H = 87.7" (Upper AV for tank fill)
AFVL L= 6830 gals (Lower AV for Inventory Control)
AFVL H = 6919 gals (Upper AV for tank fill)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 31 of 74 14.0
SUMMARY
- For 0.83 SG Fuel Oil EDG FOST TANK CAPACITY: 7693 GAL (CALCULATED REF. 3.2) 7,700 GAL (DES. SPEC.)
14.1 LOW-LOW LEVEL DISPLACER SETTING This Section addresses the LOW-LOW Level Displacer Calculated Setting For Pump STOP and Inventory Control 14.1.1 TANK 31&32 NOMINAL PROCESS LIMIT: 788 GAL (16.25" @ the pumps) (Sect. 11.2)
TRIP SETPOINT (LO-LO): 870 GAL (17.1" @ the switch ) (Unusable Fuel, Pump Protection & Inventory Control) (Section 12.1)
AS FOUND VALUE: 826 GAL (LO) (16.45" @ the switch); 915 GAL (HI) (17.75" @ the switch) 14.1.2 TANK 33 NOMINAL PROCESS LIMIT: 818 GAL (16.25" @ the pumps) (Sect. 11.2) 910 GAL (17.1" @ the switch) (Unusable Fuel, Pump Protection & Inventory TRIP SETPOINT (LO-LO):
Control) (Section 12.1)
AS FOUND VALUE: 866 GAL(LO) (16.45" @ the switch); 956 GAL (HI) (17.75" @ the switch) 14.2 LOW LEVEL DISPLACER CALCULATED SETTINGS (Alarm prior to FSAR/TRM minimum value, Operator to Initiate Tank Refill)
This Section addresses the LOW Level Displacer (Alarm) Calculated Setting Based on 6804 gallons @ 0.83 SG 14.2.1 TANK 31 & 32 NOMINAL PROCESS LIMIT: 6804 GAL (86.585" @ the switch) (Sect. 11.3.1)
ALARM SETPOINT (LO): 6874 GAL (87.55" @ the switch) (CCR ALARM)
AS FOUND VALUE: 6822 GAL (86.85" @ the switch) (Sect. 13.2.1) 14.2.2 TANK 33 NOMINAL PROCESS LIMIT: 6804 GAL (86.004" @ the switch) (Sect. 11.3.1)
ALARM SETPOINT (LO): 6874 GAL (87.05" @ the switch) (CCR ALARM)
AS FOUND VALUE: 6830 GAL (86.4" @ the switch) (Sect. 13.2.2) 115 GALLONS IN EDG F.O. DAY TANK IS NOT CONSIDERED FOR THIS FUNCTION INTHIS CALCULATION
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 32 of 74 14.3 DIPSTICK MEASUREMENT READING TO ASSURE COMPLIANCE WITH FSARlTRM INVENTORY 14.3.1 TANK 31 & 32 NOMINAL PROCESS LIMIT: 6647 GAL (87.7- @ the sounding tube) (Sect. 11.1.1)
MIN SOUNDED READING: 6682 GAL (88.2" @ the sounding tube) (Sect. 12.3.1) 14.3.2 TANK 33 NOMINAL PROCESS LIMIT: 6688 GAL (88.9- @ the sounding tube) (Sect. 11.1.1 )
MIN SOUNDED READING: 6726 GAL (89.4' @ the sounding tube) (Sect. 12.3.1) 14.4 INDICATOR READING TO ASSURE COMPLIANCE WITH FSAR/TRM INVENTORY 14.3.1 TANK 31 & 32 NOMINAL PROCESS LIMIT: 85.2u @ the Indicator or 6538 gallons @ SG 0.86 (Sect. 11.1.2 & 12.3.1) 14.3.2 TANK 33 NOMINAL PROCESS LIMIT: 85.95" @ the Indicator or 6579 -gallons@ SG 0.86 (Sect. 11.1.2 & 12.3.1)
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 33 of 74 15.0 EDG F.O. STORAGE TANK FIELD CALIBRATION CONSIDERATIONS 15.1 LEVEL SWITCH DISPLACER CALIBRATIONS The following is based on field measurements (Att. 4.15) using the bottom of the tank as the reference point, as shown on drawing FP 9321-05-2990-0. It is not always practical to measure the displacer positions while they are in the tank, but it is possible to use the mounting flange as the reference and measure how far down the displacers are to be set on the activating cable. Field measurements were made to determine the distance from:
Flange to Tank Bottom (DFTB) and Flange face to the bottom of the displacer (FFBD).
Each tank has a slightly different mounting flange dimension, so each DFTB and FFBD is different.
Tank Bottom to the Bottom of the Displacer (TBBD)
TBBD based upon field measurements, without access to the bottom of the tank, is calculated based upon the listed DFTB and FFBD values.
The measurement from the flange face to the bottom of the displacer (FFBD) will be determined by DFTB-TBBD 15.1.1 Field Measurement Review - Lower Displacer Setting - LOW-LOW switch setting, TS =17.1" (see Section 12.1)
Field value - DFTB Measured FFBD Measured TBBD (Design)
TANK 31 = 145.0625" 129.0625" 15.975" TANK 32 = 144.75" 128.875" 15.975" TANK 33 = 145.5" 129.625" 15.975" As-Left Tolerance = +/-0.60", As-Found Tolerance = +/-0.65" [comparison of Measured to calculated]
FOR TANK 31 FFBD = DFTB - TBBD (LOW-LOW)
FFBD 145.0625" - 15.975" FFBD = 129.0875" (calculated)
FFBD Measured = 129.0625" TBBD (measurement based) = 16" FOR TANK 32 FF8D = DFTB - TBBD (LOW-LOW)
FFBD = 144.75" - 15.975" FFBD = 128.775" (calculated)
FFBD Measured = 128.875" TBBD (measurement based) = 15.875" FOR TANK 33 FF8D = DFTB - TBBD (LOW-LOW)
FF8D = 145.5" - 15.975" FFBD = 129.525" (calculated)
FFBD Measured = 129.625" TBBD (measurement based) = 15.875" All readings are within tolerance.
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 34 of 74 15.1.2 Field Measurement Review - Upper Displacer Setting - LOW switch setting, TS =87.5" (Tank 31 & 32) & 87" (Tank 33) (see Section 12.2)
Field value - DFTB Measured FFBD Measured TBBD (Design)
TANK 31 = 145.0625" 61.5625" 84.1" TANK 32 = 144.75" 62.75" 84.1" TANK 33 = 145.5" 62.0" 83.55" As-Left Tolerance = +0.60", As-Found Tolerance = +/-0.65" [comparison of Measured to calculated]
FOR TANK 31 FFBD = DFTB - TBBD (LOW)
FFBD = 145.0625" - 84.1" FFBD = 60.9625" (calculated)
FFBD Measured = 61.5625" TBBD (measurement based) = 83.5" FOR TANK 32 FFBD = DFTB - TBBD (LOW)
FFBD = 144.75"- 84.1" FFBD = 60.65" (calculated)
FFBD Measured = 62.75" TBBD (measurement based) = 82" FOR TANK 33 FFBD = DFTB - TBBD (LOW)
FFBD = 145.5" - 83.55" FFBD = 61.95" (calculated)
FFBD Measured = 62.0" TBBD (measurement based) = 83.5" Prior field measurements for Tank 32 are not within As-Left tolerances for the alarm setting.
15.2 Conclusions From Field Measurement Review 15.2.1 All AS-Left Measurements for Tanks 31, 32 & 33 LOW-LOW LEVEL settings are within the ALT requirements for the switches (see Section 8.1.5). Therefore, the pump protection and inventory control functions of the LOW-LOW Level switch are satisfactory.
15.2.2 All AS-Left Measurements for Tanks 31 & 33 LOW LEVEL settings are within the ALT requirements for the switches (see Section 8.1.5). Therefore, The Alarm function (6804 gallons) will identify to Operators that action is required to initiate tank refill.
15.2.3 The AS-Left Measurement for Tank 32 LOW LEVEL setting is not within the ALT requirement for the switch. Therefore, the field setting (TBBD) needs to be changed from 82" to 84.1" to provide the required Alarm Function (6804 gallons) to properly identify to Operators that action is required to initiate tank refill. The action, to implement this setting change, is required to implement the Technical Specification Amendment change.
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 35 of 74 Gallons oH (In)
TABLE 1 - EDG Fuel Oil height in tank at devices for specific gallons Slope Effect on Measurements for EDG Fuel Oil Storage Tanks No. 31, 32 & 33 H (In) @S. H (in) @S. H (In) @L H (In) @L H (In) @ H (In) @ H (In) @L H (In) @L Tube Tube SW SW, PMP, PMP, IND IND TK31,32,33 TK31,32,33 TK131 &32=H TK33=H 0 TK31 &32=H TK(33 =H @ TK31 &32-=H TK 33=H @ TK31 &32 =H TK. 33=H @
@ CL @ CL @ CL +1.6875 CL +2,2831 @ CL-1.6458 CL-2.2267 @ CL-1.2708 CL -1.7194 @ CL +.6250 CL +.8456 175.96 6,435 8.1225 8.7181 4.7892 4.2083 5.1642 4.7156 7.06 7.2806 271.21 8.58 10.2675 10.8631 6.9342 6.3533 7.3092 6.8606 9.205 9.4256 378.99 10.725 12.4125 13.0081 9.0792 8.4983 9.4542 9.0056 11.35 11.5706 497.78 12.87 14.5575 15.1531 11,2242 10.6433 11.5992 11.1506 13.495 13.7156 626.36 15.015 16.7025 17.2981 13.3692 12.7883 13,7442 13.2956 15.64 15.8606 704.44 16.25 17.9375 18.5331 14.6042 14.0233 14.9792 14.5306 16.875 17.0956 717.3 16.45 18.1375 18.7331 14.8042 14.2233 15.1792 14.7306 17.075 17.2956 755.3 17.0208 18.7083 19.3039 15.375 14.7941 15.75 15.3014 17.6458 17.8664 760.06 17.1 18.7875 19.3831 15.4542 14.8733 15.8292 15.3806 17.725 17.9456 763.66 17.16 18.8475 19.4431 15.5142 14.9333 15.8892 15.4406 17.785 18.0056 784.5 17.4694 19.1569 19.7525 15.8236 15.2427 16.1986. 15.75 18.0944 18.315 787.51 17.5208 19.2083 19.8039 15.875 15.2941 16.25 15.8014 18.1458 18.3664 795.875 17.6458 19.3333 19.9289 16 15.4191 16.375 15.9264 18.2708 18.4914 812.6 17.8958 19.5833 20.1789 16.25 15.6691 16.625 16.1764 18.5208 18.7414 817.58 17.9694 19.6569 20.2525 16.3236 15.7427 16.6986 16.25 18.5944 18.815 826.1 18.0958 19.7833 20.3789 16.45 15.8691 16.825 16.3764 18,7208 18.9414 844.69 18.3708 20.0583 20.6539 16.725 16.1441 17.1 16.6514 18.9958 19.2164 851.91 18.4767 20.1642 20.7598 16.8309 16.25 17.2059 16.7573 19.1017 19.3223 863.43 18.6458 20,3333 20.9289 17 16.4191 17.375 16.9264 19.2708 19.4914 A 865.53 18.6767 20,3642 20.9598 17.0309 16.45 17.4059 16.9573 19.3017 19.5223 870.3 18.7458 20.4333 21.0289 17.1 16.5191 17.475 17.0264 19.3708 19.5914 875.3 18.8194 20.5069 21.1025 17.1736 16.5927 17.5486 17.1 19.4444 19.665 884 18.9458 20.6333 21.2289 17.3 16.7191 17.675 17-2264 19.5708 19.7914 908.84 19.305 20.9925 21.5881 17.6592 17.0783 18.0342 17.5856 19.93 20.1506 910.33 19.3267 21.0142 21.6098 17.6809 17.1 18.0559 17.6073 19.9517 20.1723 915.17 19.3958 21.0833 21.6789 17.75 17.1691 18.125 17,6764 20.0208 20.2414 924.27 19.5267 21.2142 21.8098 17.8809 17.3 18.2559 17.8073 20.1517 20.3723 955.79 19.9767 21.6642 22.2598 18.3309 17.75 18.7059 18.2573 20.6017 20.8223 1061.23 21.45 23.1375 23.7331 19.8042 19.2233 20.1792 19.7306 22.075 22.2956 1220.04, 23.595 25.2825 25.8781 21.9492 21.3683 22.3242 21.8756 24.22 24.4406 1384.69 25.74 27.4275 28.0231 24.0942 23.5133 24.4692 24.0206 26.365 26.5856 1554.72 27.885 29.5725 30.1681 26.2392 25.6583 26.6142 26.1656 28.51 28.7306 1729.62 30.03 31.7175 32.3131 28.3842 27.8033 28.7592 28.3106 30.655 30.8756 1908.75 32.175 33.8625 34.4581 30.5292 29.9483 30.9042 30.4556 32.8 33.0206 2092.16 34.32 36.0075 36.6031 32.6742 32.0933 33.0492 32.6006 34.945 35.1656 2278.16 36.465 38.1525 38.7481 34.8192 34,2383 35.1942 34.7456 37.09 37.3106 2467.43 38.61 40.2975 40.8931 36.9642 36.3833 37.3392 36.8906 39.235 39.4556 2659.62 40.755 42.4425 43.0381 39.1092 38.5283 39.4842 39.0356 41.38 41.6006 2854.41 42.9 44.5875 45.1831 41.2542 40.6733 41.6292 41.1806 43.525 43.7456 3050.62 45.045 46.7325 47.3281 43.3992 42.8183 43.7742 43.3256 45.67 45.8906 3247.93 47.19 48.8775 49.4731 45.5442 44.9633 45.9192 45.4706 47.815 48.0356 3446.93 49.335 51.0225 51.6181 47.6892 47.1083 48.0642 47.6156 49.96 50.1806 3646.55 51.48 53.1675 53.7631 49.8342 49.2533 50.2092 49.7606 52.105 52.3256 3846.45 53.625 55.3125 55.9081 51.9792 51.3983 52,3542 51.9056 54.25 54.4706 3900.04 54.2 55.8875 56.4831 52.5542 51.9733 52.9292 52.4806 54.825 55.0456 4046.34 55.77 57.4575 58.0531 54.1242 53.5433 54.4992 54.0506 56.395 56.6156 4245.96 57.915 59.6025 60.1981 56.2692 55.6883 56.6442 56.1956 58.54 58.7606 4444.97 60.061 61.7475 62.343! 58.4142 57.8333 58.78921 58.3406 60.685 60.9056v 58.7892 58.3406 60.685
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 36 of 74 TABLE 1 - EDG Fuel Oil height in tank at devices for specific gallons Slope Effect on Measurements for EDG Fuel Oil Storage Tanks No. 31, 32 & 33 Gallons H (In) H (In) OS. H (In) OS. H (In) @L H (In) CL H (In) @ H (In) @ H (In) @L H (In) OL Tube Tube SW SW, PMP, PMP, IND IND TK31,32,33 TK31,32,33 TK31 &32=H TK33=H @ TK131 &32=H "K33=H @ TK31 &32=H TK 33=H @ TK31 &32 =H TK. 33=H 0
@ CL 0 CL @ CL +1.6875 CL +2.2831 @ CL-1.6458 CL -2.2267 @ CL -1.2708 CL -1.7194 @ CL +.6250 CL +.8456 4642.27 62.205 63.8925 64.4881 60.5592 59.9783 60.9342 60.4856 62.83 63.0506 4838.49 64.35 66.0375 66.6331 62.7042 62.1233 63.0792 62.6306 64.975 65.1956 5033.27 66.495 68.1825 68.7781 64.8492 64.2683 65.2242 64.7756 67.12 67.3406 5225.47 68.64 70.3275 70.9231 66.9942 66.4133 67.3692 66.9206 69.265 69.4856 5414.73 70.785 72.4725 73.0681 69.1392 68.5583 69.5142 69.0656 71.41 71.6306 5600.73 72.93 74.6175 75.2131 71.2842 70.7033 71.6592 71.2106 73.555 73.7756 5741 74.567 76.2545 76.8501 72.9212 72.3403 73.2962 72.8476 75.192 75.4126 5780 75.026 76.7135 77.3091 73.3802 72.7993 73.7552 73.3066 75.651 75.8716 5784.14 75.075 76.7625 77.3581 73.4292 72.8483 73.8042 73.3556 75.7 75.9206 5963.27 77.22 78.9075 79.5031 75.5742 74.9933 75.9492 75.5006 77.845 78.0656 6121 79.153 80.8405 81.4361 77.5072 76.9263 77.8822 77.4336 79.778 79.9986 6137.22 79,353 81.0405 81.6361 77.072 77.1263 78.0822 77.6336 79.978 80.1986 6138.17 79.365 81.0525 81.6481 77.7192 77.1383 78.0942 77.6456 79,99 80.2106 6160 79.638 81.3255 81.9211 77.9922 77.4113 78.3672 77.9186 80.263 80.4836 6168.73 79.7458 81.4333 82.0289 78.1 77.5191 78.475 78.0264 80.3708 80.5914 6176.21 79.8384 81.5259 82.1215 78.1926 77.6117 78.5676 78.129 80.4634 80.684 6191.48 80.0294 81.7169 82.3125 78.3836 77.8027 78.7586 78.31 80.6544 80.875 6199.64 80.133 81.8205 82.4161 78.4872 77.9063 78.8622 78.4136 80.758 80.9786 6201.31 80.1544 81.8419 82.4375 78.5086 77.9277 78.8836 78.435 79.5294 81.0 6208.89 80.25 81.9375 82.5331 78.6042 78.0233 78.9792 78.5306 80.875 81.0956 6215.04 80.3267 82.0142 82.6098 78.6809 78.1 79.0559 78.6073 80.9517 81.1723 6216.32 80.3428 82.0303 82.6259 78.697 78.1161 79.072 78.6234 80.9678 81.1884 6218.87 80.375 82.0625 82.6581 78.7292 78.1483 79.1042 78.6556 81.0 81.2206 6220.52 80.3958 82.0833 82.6789 78.75 78.1691 79.125 78.6764 81.0208 81.2414 6231.11 80.5294 82.2169 82.8125 78.8836 78.3027 79.2586 78.81 81.1544 81.375 6238.15 80.6184 82,3059 82.9015 78.9726 78.3917 79.3476 78.899 81.2434 81.464 6240.999 80.6544 82.3419 82.9375 79.0086 78.4277 79.3836 78.935 81.2794 81.5 6248.55 80.75 82.4375 83.0331 79.1042 78.5233 79.4792 79.0306 81.375 81.5956 6254.68 80.8277 82.5152 83.1108 79.1819 78.601 79.5569 79.1083 81.4527 81.6733 6258.406 80.875 82.5625 83.1581 79.2292 78.6483 79.6042 79.1556 81.5 81.7206 6266.41 80.9767 82.6642 83.2598 79.3309 78.75 79.7059 79.2573 81.6017 81.8223 6308.2 81.51 83.1975 83.7931 79.8642 79.2833 80.2392 79.7906 82.135 82.3556 6472.86 83.655 85.3425 85.9381 82.0092 81.4283 82.3842 81.9356 84.28 84.5006 6631.66 85.8 87.4875 88.0831 84.1542 83.5733 84.5292 84.0806 86.425 86.6456 6636.77 85.8705 87.558 88.1536 84.2247 83.6438 84.5997 84.1511 86.4955 86.7161 6642.23 85,9455 87.633 88.2286 84.2997 8317188 84.6747 84.2261 86-5705 86.7911 6649.46 86.0455 87.733 88.3286 84.3997 83.8188 84.7747 84.3261 86.6705 86.8911 6651.23 86.07 87.7575 88.3531 84.4242 83.8433 84.7992 84.3506 86.695 86.9156 6668.36 86.308 87.9955 88.5911 84.6622 84.0813 85.0372 84.5886 86.933 87.1536 6669.49 86.35 88.0375 88.6331 84.7042 84.1233 85.0792 84.6306 86.975 87.1956 6671 86.3705 88.058 88.6536 84.7247 84.1438 85.0997 84.6511 86.9955 87.2161 6698.24 86Y7255 88.413 89.0086 85.0797 84.4988 85.4547 85.0061 87.3505 87.5711 6707.14 86.8505 88.538 89.1336 85.2047 84.6238 85.5797 85.1311 87.4755 87.6961 6716.72 87 88.6875 89.2831 85.3542 84,7733 85.7292 85.2806 87.625 87.8456 6721 87.059 88.7465 89.3421 85.4132 84.8323 85.7882 85.3396 87,684 87.9046 6728.07 87.1458 88.8333 89.4289 85.5 84.9191 85.875 85.4264 87.7708 87.9914 6741 87.319 89.0065 89.6021 85.6732 85.0923 86.0482 85.5996 87.944 88.1646 6742 87.342 89,0295 89.6251 85.6962 85.1153 86.07121 85.6 2 2 6 87.967 88.1876
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 37 of 74 I TABLE 1 - EDG Fuel Oil height in tank at devices for specific gallons Slope Effect on Measurements for EDG Fuel Oil Storaae Tanks No. 31. 32 & 33 Gallons H (In) H (In) @S. H (In) @S. H (In) @L H (In) @L H (in) @ H (In) @ H (In) @L H (In) @L Tube Tube SW SW, PMP, PMP, IND IND TK31,32,33 TK31,32,33 TK31 &32=H TK33=H @ TK31 &32=H TK33 =H 0 TK31 &32=H TK 33=H @ TK31 &32 =H TK. 33=H 0
@ CL @ CL @ CL +1.6875 CL +2.2831 @ CL-1.6458 CL -2.2267 @ CL-1.2708 CL -1.7194 @ CL +.6250 CL + .8456 6743.47 87.3717 89.05928 89.65488 85.72598 85.14508 86.10098 85.65238 87.99678 88.21738 6754.97 873519 89.2065 89.8021 85.8732 85.2923 86.2482 85.7996 88.144 88.3646 6757.54 87.57 89.2575 89.8531 85.9242 85.3433 86.2992 85.8506 88.195 88.4156 6762 .87.6323 89.3198 89.9154 85.9865 85.4056 86.3615 85.9129 88.2573 88.4779 6762.94 87.6458 89.3333 89.9289 86 85.4191 86.375 85.9264 88.2708 88.4914 6781 87.902 89.5895 90.1851 86.2562 85.6753 86.6312 86.1826 88.527 88.7476 6782.77 87.9268 89.6143 90.2099 86,281 85.7001 86.656 86.2074 88.5518 88.7724 6784.05 87.945 89.6325 90.2281 86.2992 85.7183 86.6742 86.2256 88.57 88.7906 6787.59 87.9958 89.6833 90.2789 86.35 85.7691 86.725 86.2764 88.6208 88.8414 6794.46 88.1024 89.7899 90.3855 86.4566 85.8757 86.8316 86.383 88.7274 88.948 6799.94 88.174 89.8615 90.4571 86.5282 85.9473 86.9032 86.4546 88.799 89.0196 6800.17 88.1757 89.8632 90.4588 86.5299 85.949 86.9049 86.4563 88.8007 89.0213 6801 88.187 89.8745 90.4701 86.5412 85,9603 86.9162 86.4676 88.812 89.0326 6803.75 88.2267 89.9142 90.5098 86.5809 86 86.9559 86.5073 88.8517 89.0723 6808.56 88.299 89.9865 90.5821 86.6532 86.0723 87.0282 86.5796 88.924 89.1446 6811.24 88.335 90.0225 90.6181 86.6892 86.1083 87.0642 86.6156 88.96 89.1806 6827.89 88.5767 90.2642 90.8598 86.9309 86.35 87.3059 86.8573 89.2017 89.4223 6832.6 88.6458 90.3333 90.9289 87 86.4191 87.375 86.9264 89.2708 89.4914 6840.06 88.7574 90.4449 91.0405 87.1116 86.5307 87.4866 87.038 89.3824 89.603 A 6848.52 88.8824 90.5699 91.1655 87.2366 86.6557 87.6116 87.163 89.5074 89.728 6850 88.8998 90.5873 91.1829 87.254 86.6731 87.629 87.1804 89.5248 89.7454 6872 89.2267 90.9142 91.5098 87.5809 87 87.9559 87.5073 89.8517 90.0723 6897.28 89.6058 91.2933 91.8889 87.96 87.3791 88.335 87.8864 90.2308 90.4514 6899.98 89.6458 91.3333 91.9289 88 87.4191 88.375 87.9264 90.2708 90.4914 6929.24 90.09 91.7775 92.3731 88.4442 87.8633 88.8192 88.3706 90.715 90.9356 6936.88 90.2067 91.8942 92.4898 88.5609 87.98 88.9359 88.4873 90.8317 91.0523 6938.14 90.2267 91.9142 92.5098 88.5809 88 88.9559 88,5073 90.8517 91.0723 7066.53 92.235 93.9225 94.5181 90.5892 90.0083 90.9642 90.5156 92.86 93,0806 7195.11 94.38 96.0675 96.6631 92.7342 92.1533 93.1092 92.6606 95.005 95.2256 7313.9 96.525 98.2125 98.8081 94.8792 94.2983 95.2542 94.8056 97.15 97.3706 7421.68 98.67 100.3575 100.9531 97.0242 96.4433 97.3992 96.9506 99.295 99.5156 7516.94 100.815 102.5025 103.0981 99.1692 98.5883 99.5442 99.0956 101.44 101.6606 7597.4 102.96 104.6475 105.2431 101.3142 100.7333 101.6892 101.2406 103.585 103.8056 7659.37 105.105 106.7925 107.3881 103.4592 102.8783 103.8342 103.3856 105.73 105.9506 7692.89 107.251
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 38 of 74 Attachment 2 Page 1 of 2 Magnetrol Drawing D-1257 (FP 9321-05-7214 Rev. 0,1/22170) " Magnetrol Installation Dimensions Model A-153F-TDM & A-153-F-E.P.-TDM".
Mar #AINSTALLATION DIMENSIONS MO0CELA-1I53-F-TDM 8 A-153-F-E.P.-TDM 14 UWO 1M-D,1kw. -
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IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 39 of 74 4-FT44W4"lFAJ-r X,, A &1 2 A~~I INSTALLATION DIMENSIONS MODEL A -153-F-TOM twowa c"WCUciao A-153-F-E.IP--DM
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IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 40 of 74 ATrACHMENT 3 Gould pumps Bowl Engineering Data, # 22.13, October 1, 1986, "Minimum Submergence Required for Vortex Suppression".
lowI E W CM A T Tf de Am&,i T 22 MINIMUM SUSMERGENCE REQUIRED FOR VORTEX SUPPRESS21t RiM Iwo Ago n-ug 4 - 1. L; 7.
LE J`
7 -01;;Zj a-r7 r__,"i EiFE, p IL: 04*- 17) te, I lvi ILIL__
9ý9 L&Ar.3 Ia WU. 0Fs in isto NOT I . bbmuuN1 sEavo lab" ami VWm oft~ h"9"n%%Cthck WASiurmM~
Wto to I"UMO.9MVOS PU
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 41 of 74 ATTACHMENT 4 Telephone Discussion Documentation form, 6/5/91, A. Cerwin to T. Fricke.
MW VCORs 5muLE AUNKOtItI
)*JeIlZA1 !i~l hZEtPtlte & OLStOW SEClTIOlI "LZpmjOt DZSCUsEUoK D*7OC*07*TION FON A r."
,- z -P,%,z F -r 1-. A"
- P - eC,.L - eg* - 0103.a CALL O'TI J /?, TINE 1"O A, ~G2N.~
REThteZl '9'41;ay' Or TRE NMTHIORIY AND fc(o AN______ _____________
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IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 42 of 74 ATTACHMENTS6 Telephone Discussion Documentation form, 11/10/93, F. Granitto to D. Wilson.
~t of 1.
Erie youx MIoi MMORI1y CAL'L OAT2I OI0 9 TINE 10-Oce Vt! Ib 92"Em &OI-r~LOp &MAMJ -or tAmozv Abr* tbA*JL VALS2IbM )A~* sP.Cj¶ueV.
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IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 43 of 74 ATTACHMENT 10 U.S. Environmental Protection Agency (EPA). 1995. Review of MathematicalModeling for Evaluating Soil Vapor Extraction Systems. Office of Research and Development, Washington, D.C. EPA/540/R-95-513.
For depths greater than 100 cm, the mean annual soil temperature remains relatively stable throughou the year and can be estimated from the average shallow ground water temperatures shown in Figure 1.
....... . S hallw.*
A
,t-im - .... Va e 2 I4. . . ... . s 7' Figure 1. Average Shallow Ground Water Temperatures in the United States
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 44 of 74 ATTACHMENT 12 IP3-RPT-EDG-01 632, "Operation Graphs, TC-25A through TC-25D Diesel Generator Fuel Oil Stora~qe Tanks Slope and Specific Gravity Compensation, dated 10/21/95.
am YOMR~S AVISOPXY nEThN Por 3 WICLMA POiN= PLUM2 OJ I3AY? GR1AM I-2IAY3 YV-29D 02h2= =ATMO r= 017, ft01143 "J=K StOPS Am suzrxc QWAVTf ?IUS&Z
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 45 of 74 Z-34--MU -0163: MVW. 0
.,* -)- Lsvtc_- SO*- o#*t,
.1 Thbis tedprt provda th-. -oc*umsnt:ataic of tho muuchod,, yl, uAed to corre¢.c the 11, 2 & 33 lieesqi *Omeerator Fuel 1t. st.rage rank Inc..h vs. GeJloa GraPhs loperatiama Gras r-2A,-151.,-2k & -
MlD. Th* oaigiial graph. operation C*raph ¶C-2s was based n calcL]atioa 200 Whlch does not 0o911daV thnA ;lope.
21 'mecqvnc-y Diesel C*efrator igmGI Lv'e'. *t*dicators Li-li)], LI-1:31 and LI-tIJ are calibrated for 310. 2 deseal vel writ, a specific gravity of 0.0,. ThL. report detaitg*ls tbe j'th,*dodLt of when and how* the irbdlca tori can b* c4-pyet1Sattd for a change in
- pa'cific gravlty.
Calcyaltion 200. Di~afnl Genoratao Fuel Oil Stnraffe TamnX Capacity calculatLon tfl periorned Co prochc* a gra3b of l"l Vers*us v'IWse of finl oil contaigied to the emDO fEl stot*ae t*eks. This iof*matios was themn %ed to prGduce Op~rAtions =raph tiTC-25 Rev 0 Th EDO f'4el h il storage tanks arne desigrnd to be Inseadaod wvtb a J) slope over a srking distance at Io4' 2" distate freferAhs drawing L3v-33-60e21.
With this dmeiw slope the bcminhl levet at the veetlcal ceatertine of the tonk yields 1e21el VAlues wtaett can be comvertod to gallons usla ca]cViutioa 200. -1* unsure the nominal lwevl of the diaiel rue:m pit
~the loel irmdicvnr zeadi*v;s and the dip stick reqAýngu nn4 to b-0 corrected1 to a -- ;tqr~i0m lbl 4Aqivalint to cco*pnmaatm toor rL lopa. Calculation 200 aw4 not-co.l*er cank slope L'Wrift the irylementat~ion of OW *4-)-132 100 *.v,l atcual slope peesurefhos wiere takem for at] tbree kra fuel oil tank* (see Attacluwnt 11. UsinG these maGAuri,*emnt-s "as built' 426 rnrrecti,*-
factors nrc deterinsd. The followiAg rarreccl*a factors wet. o ied toa thie level indicatogr and digsLtiCx gWhhUrauontS to oq~Alit cbe eq~aivalen~t taok centerline slevatiaan:
31 KG il Pad torfe TnocCml Indicutor Dips tick 31 tVG riel Oil Storaqv T0amX U5S 1.628" 32 ED Padl Oil $tvrege lank 0.625, L.19u" 33 RCX Fuel Oil S",reae Tank 0 u45" 2.2S3" W'hen tWsvO;Dic the nev graphs the inCh 76 ge1l eCUXr, I M5 oJffnuL by che abowe factors sines the level irdicmt.r aM dipstick raoeings indicate wmre Fil due co the tank slaps, This was accoplishsd by adding the corroetian eCtorsr. L he K cWlCI a* omtTaChMet 2 of CaLculaticc 200 Sinco there are different cozructtcmn facaors reoquiryd for the levvl indicator aind th: dlptif-cx, iapante curvas wore .trAzratd. Tn, addiriobn sepraLe etpr-ue were zaqired becmuee the corxection factors for 7fF*el Oil Storage,?*k 3l and 32 wore different chfn fat rank 33. Attachmant 2 is the tabl*14ed tich vs g411onE tables .orrected for Tank slaopl u;sed to develop t-1h
- Age I OF 3
1P3-CALC-EG-0021 7 Rev. 5 EC-32406 Markup Page 46 of 74 np~re ITArhS -Mp~.T-JSA. -353. -25C an~d -25D.
Operatimns qrwavbu W-25A thrcj.:gh WC-250 in~dicate oominek leve! mnd rRqflect tM.. actual. oamountfl NC oil i thUe staC!ge LAJkak based cm a reading that is correcetod to theO level rpromnted at tank cmnterlIr.i@
V=~ UPzel Oil. Louel Ii-iL-Catas -,1-1031. Lt-t34 anti 1L-213S bavt a calibrated #r*9 t4or t'aeL oal w.mtb a £2pacific grawit-V 1$% og0.6 tlie AllJW4blf -04'x~an, for do. 2 biamami f-il oil in e3 to .B9.
T-n ord1er to de'rormirA. the fuel ULl leVOl CO Lh4 ISOa gallohp, jnptrvaPqei 1
aecura~y, Cbs E6lL64.itV 0*92L1tc"~ Er w1pocific gravity deviation oust KAULI~a Cooaiia'e4 _______ i nch reading level in jachwa currwn 05 value 71he SG cumpem-sted gSallqI rooding c".a thpen be obtained by u~l1itioq t.)jo "Vroorlate ciperationa 03&Dmb 4?C-2se Or Tr'.261D.
tla Lbe Dhht 5 year 5 tbe 68 barn niot deviated. by acti tbhaq t 0O1. *1,Thl V translate. to a wcar*t~ "so* Pp*eikl. error ot 150 galloon. Te alleviace U~r&LL~an parnonzael MARoaAP~lYi.g a SQ comawsat~eqi to the level 3.~icatlon reading tho tollwing has been aMplied:
It Cho acctual 83 L2 belcwi 0.91 tb* level +/-ndicar.-Pro WUL iodicate 'eve tual thlan in actually in the tanX. Sinc~e the 1idIicator %*&dng!A is ka LbA co~axa~~l~ve dizactLon, no CorK*E~i45ft Is requizred If t ~CIs above 0.86 the indicatozs will inidicate mrire bjei. tbanI .15 V.1.
a-tvially ;,n thae tank. To tirog~ensate for this codi~tioe. 1SO pa~llafs .2(
oil Ihas been aidded to r-be TaolUalcA $pc~iicwtiin rmqired level. ntis 150 gallce accouts fuar a 8C3 deviation u~p to D..D¶2. Xuami z.)uah the highaat SG Ya1lu* observad Iin LbA Past 5 yosr* wa D,972 thes jlloistble
- S romge is .43 t.p -69. it 0e PG go-es above 0.8732 ';.n1ndicAcor reziling wast be compensnated far SG or the: t-abko em~p bip sia"JVwa aqwndeA tp onomir* that the rvnmirel Spc~ification raqpirafnmatz of cor~d 9the frun! has beeno met. Cbamistry proo-oduo MRf-C:A-0415 rieyires t'ýWt.
Contcir;. 3toc Supervisor arid thle P.L~ft maniager be nDCL114d it tCje
.*corded 90 Is greater thani U.972.
CaTWI119MVU Operations g2raphs5 2C-21A -21D. -25'C and -25D xaflwes rmcbLnal level.
the c-.arv,.z havekam ~atn*du~tvi to ccoUyps.te tor this ac-rial t~amk rloi:.i. Calculation 200. Dies-el Clenerator Fuiel oil a rssatak.
Capnmrity calculation doom hot convidler tciik slope. Attachment 2 of Calculation 200 Vai adjusted for bot.h ch* 1sv*1 ind.L.tALazx And apatick
-uudirLgu toa cimpooMALLu for tank ICW I= lorvul irx Ataz L1-1133-1i134 ana -]%)I are calibrated for NIo. 2 fuel oil w.ith a So of 0 66 Mhe specific gravity <caa vary beewuman .133 page 2 OF 3
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 47 of 74 zl-Mn-umG-0t112 %-I-T'diPA.-SJ9'eJI
(--0-L . 0C C-c- (a.
OatC 7
- 69. To mqssarw tl% fumta *LC to tbe *S0 gal2on. i
,8d -amtr .4 i zeutaaey the Ilnd-catcr reading wrst be compensated for SCG doevrtatn trom 0.06. i4. the sm dwcp bwlov 0.66 a eaceraetLan Is not roquired bqcauo the level uidicacor will rea*d conmenratiwly, Fcr SO drisltinc between 86W end 672, no Sr c~oecsvennhlo La requtrsd because L50 ygm I lame fI fuil was added to the ?Jtcbnlci Specif!cation level reuinreoencu to uccount Inx tbs VosoLbla *,trot due to the laceiesse or.
5G. Vr = qzaraer than 0.972 the Ievel idicator reading m**t be ccapensated tur So deviutiom qt the S00 fucl oil qtceage LikA*sl buat be manLnually *egndqid to e ns*re Technical Specification raquireants.
Vais intormotion volJ bes U4j'lI2 to teasoln ACTS hhmaabr 1344.3.
calcultatica T-CALC-BG-01211 did not consider the tank slope Wien atersrimlng tbe -juiuablq fuel vvzlao wthbf 4*totmirting the On2 St~oagi Tanks seepolats.
tewemmucol:
SWIMP9-3-l12 KVm RAW. 1 Plv3-439-1390 Rev. I Calculavion 200 qperahtions Graph TC-251 Rev, 0 Operationa rJwpb rc-25A 0 oJp40rati~n~a Graph TC-259 e*Y.
Operationu cmap-b -Z-5C Rev.
Qlraetiom Csohi TC-25D Mg9 3 CS:3
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 48 of 74 S aI .
9o AoA&'- T**kL S&-QG-LA 4 eqnItP~r
/ e.UAJIIAJ
- - I -~ *b. LSbdt
-4 At o tli/smI tvIs tts I.
t Mfl0eA,- $tyi0a4 Ot-sm~op 4 Li1 ! Ot Pk II-1443-,
v I ftas" Con. FcIbt.S &.rP..aaJ So~o,tIj tIj Cr flub %MA
'I 2-
'C Q.M.A rn-tin &nsffA&) %-I* 4t,4v. 42'%
t (44%
8 ts6r I
?'~c iti~~ 13
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 49 of 74
- J's~.
7,19 M.5-r Acyvmw. Ar. s.6r 0"9t- Gt& PO rAk.#. 3 t..
-WI- &
_VL - ,.t
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ii, =.7,4t0i",
ip
-r d" I. 66S I, ?q4-Arwnt- Cost. b.4-cTmt. F'- T^**- e 5j;.aJ$A Ar
('go&~*1 ,4 j.LjJ, 4l wV~
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 50 of 74 4 rP3-F V t4LC 6,- pf.P jg
.00 Amp.- -lik t- Cý&w G."l*L-IN- 1n11 De. ')d1/4 Momvep Ca~cr'o' Rqfl 6'-*aj CIdwPmjb shWtr 4k Vr,-DrLt'flV,-A 1.+ ?4.Ifc 00n FAhcWJL WrLAA' SOMPe.Atvn6 A~b 'P 4 - m Con rAW,.trnjakj LT-A Z4t45- IANj A1AcsIA0c 1 Pw 3 ar-
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 51 of 74
_r
- 03. M5
'5.5 5.971 0 ,6 A 7re.#ff-Yftr*11~ VA
.75-96 0)
- 71.21 *,.413) 'S.
J18.99 197.17 14.ssV 15-A4 k
- 26.36 16; .ýr0 4;63.6S L.9841
)GIN. B4 20. 91 23.139 0 ius &~!M'II %rZ5A
.330.04 2S. 281 ~w. C L36I4.9 27. 424 SS4.72 29.513 31.7?18
.- 2942 3)) #4
.901.7E 3,6 -CC 34,009
?2"16. LS 40 .109
!447.43
- 659.62 42.141 9IS4.4t 44.5$8 1050 .6 4".733
)247.93 48,178 *4v~~
1446.93 11 .U23
$64t. 55
- 144,45 55.313 m huu.ivr z 3*.451 1046.34 L245.96 144,4.97 61.749 3642.27 6;) 0493 16i ,49 66.031 3033.27 64,103 S225.47 70.328 3414.73 '72.413 00 74-i18 i4 . 73 1754.14 59(3.37 7a .903 i138.17 31 .053 43016.2 3.42 9353. ZL9 S412.06 6631.64 87.488 "1184. 05
- 92S.24 91.778 93.9z 1195.11 96 0*t
- '313.*) 9l.213 T421 .68 1OO.356
?516 .94 14a2-503
)397.4 104,646 7459.37 "0a6.793 1666. 91-04 ilo, is
- 4 %I~4.$1 h .*M~.eI b~
jnqCHNOkT t.
9hba- t.I
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 52 of 74 GALLA-AS L4ft
,k4s 0.125f" 33.05q ".. .---------------- *--
2.77 4 *15 193*-
ITS . S I; I1.06 "q I4 £4LL- * / -J,-I7 271.21 9.205 378,91 1l.35 437.75 13.4S5 o~eS.rtu$
626.36 15.64 l5 .1*5 17 .ls4 763.66 19.93 1061,23 22.'37S 1220.04 26.22 13$4.6 26.365 28 51
&0v.
0 1554.72 1729,. 62 30.655 326s 34.945 22"8.14 2467.43 39.2315 26*99.4a2 41 .)8 2654.41 4S .525 3050.62 4'S. 41Is 3247,93 3446-43.
47.115 itUism,uC F%4' Q~w4AACLSmP4J Z 40,.91 3946.55 52.105 3946-4S 54.25 4044.34 56.395 424S.96 53.54 4.44.97 60.69$
4642.27 62.81 4098.49 64 .975 5033-27 67. 1i 5225.47 69.26S 5414. 73 71.41 5600.73 7*.sSS 57!4.14 7577' 71 .845 5963.27
!fill.II 46308.2 6472.16 663%166 86.425 6754.05 86. 57
- 90. 715 7044.S1 go 92 -Offs 7195.11 9S 7313.9 97 lS 7421.68 99.29S 7511.94 101,44 7 ,*197.4 10)5*5 659-.37 105.73
- 1603.12 1"r 107. 25
- vI 7wabý.Iz1 !"1,094 Cry .41.1 ý. 1114.
4VnscnWcut 2.
CueMO r-4
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 53 of 74 4IAL LA39 33.0 ............ .. 4.
- 429
,-, - ---- --------- rT? £*,~ ;,*j S 5"T) 4 115,94 6.715 -P3 "4LC. - C&p -
10 .16 1 t t 271.22 378,99 13. 30S 497.78 15 153 626.36 11~.29S 8r ~
763.566 908.84 19 21.599 443 9 0' IAH -Cac 1061.23 23.373 1220.04 0.84.69 21 .02) tS14,72 31 .165 1129..2 1198.75 34.459 2092.14 16.602 2275.16 38.746 2461.43 40.9093 2659-62 43.036 2354.41 45 111 !r Ii ibtsE FAWg Cdtt4.u.A-fTA 3050.52 47.328 49,471) UcI, e- -
)247,93 3446-93 51.618 3646.$S5 53.74) 3646.4s 95 .908 4046.34 51.053 4245.96 60.2ts 4444.97 62.343 4642,27 64,486 436.849 66.633 5033.27 5225,? 10. 923 5414.73 73 0460 5600.713 7S.213 77 351 5963.2? 79.S53 4131.17 81 648 6300.2 83.793 6472.86 BE .936 1631.46 68.00)
Efl54.05S 9D .229 69*9.24 93.373
?066.92 94.SL18 7195.21 96.663
?)*13 It
?422-66 100-M5 7514,94 103.098 7991 .4 la]s.243 7655.,6 AIL 10"r. 25
- 4. ?4*S2G "I'ud by ivrpo4aiiej AlrvCAVF I-er0C- jz004
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 54 of 74 8s't .)
aALLOWS rs.%4 Q *........
2.90 ,I7rT4MA1J~iN7T ;x-5.E 5.135 7-29 XIP-3LAIL-C .).1' A0.t 91.429 is of AC 11.57
"-76 "97.76 15.167sD#T 126.14 "63.66 141.005 00.04 4TtrwU$ GPA#RK W2Sb-4t)
.061.23 22.295 3m, 2 4. iw 4.q 554.72 26.71
.729.62 30.975
.900.75 J3.02
- 092- 16 35.165 1210.14
- 447,43 39.45S
!954,41. 41.6 43 .745 3054.42. 45,,,
&J47.53*
IDSO.13 48.035-tq 1.446.93 50:, .1$ Ok'w FfrOJI CM wm 41 J4)S
,646,55 53.325 2-1046.14 5,6.515
- 24S.94 !5$. 7,6
-444.-97 0. 05
- 442,.27
.A38.49 6S +L9$
i0)) ,27 67.34 69.45 i22I .47 65.J.95
- 414. 73 67I. "
A$00.73 73.771t 15.92 "S.06S 60 fl A12,
- )03 -$6'1
.2 82.355 04.5 3631.66 5794.05 89.79 929.34 00.9135 066.53 93.08
'lfl.11 97.31 "13 -9
'421.60 99.516 1316.94 101.66
'597 4 105.90
'655.31 10745
) 7 P. 49 -4
-*$- 701-C1 A?'SI8wLr7 2.
k~r- 4, OF-A'
IP3-CALC-E%0217 Rev. 5 EC-32406 Markup Page 55 of 74 31 & 32 DIESEL GENERATOR FUEL OIL STORAGE TANK TC-25A WIqTVWeq Wt J~n PFtC
" 1E6q.AiLD INCHES OIL vs. GALLONS OIL (CHART FOR DIP STICK INCH READING ONLY) 110 "l
IL-t.
fk- l 1000 '1500 2000 200 0ta "D 3500 4000 4500 WO00 5*50 60m 6500 7000 7500 00 COPY GALLONS CURVE COMPENSATES FOA TANK SLOPE
IP3-CALC-oo,,0217 Rev. 5 EC-32406 Markup 0 74 06aof 31 & 32 DIESEL GENERATOR FUEL OiL STORAGE TANK TC-258 Ptq a WtEVI . r -.
C r INCHES OIL vs- GALLONS OIL PuenNAVEYD.E (CHART FOR LEVEL INDICATOR INCH READING ONLY) ,___M__ eOA IF THE SPFC:IFfC 8RAVW" lEG) OF THE DIESEL "'*L ,. .-OI72 THEN THE Lf*lt, INDCATIOR INW)"
READING eusr BE CORRECTED FOR s6.
110 . ..... -.. -Z
- 0 1l T. IJ
..... . " . .... F ..... .. .... .. .. .. '"
- 8 ., ....-.I ----- ~---.--, -Ij , ,
- I I_
_-+ _
-J . --..-.....
.I ...
0 ..
307 9 j......-I--. ' .. ....
0k~*KIE "*3IaCRE*G CULI*FFAN 10i !-....... ...-- ..... ..i..... . . .
0 500 1000 1500 2000 2500 3000 3600 4000 4600 6000 5500 6000 6600 7000) 7500 6O000 TO CO~fREI1 IC(I 8&GAPPFY THIGAOS F0Lou*,. ALON O PDIICUM.TI iI U lJ ii.".aa OiR LI-1,0d CURVE COMPE*NSATE$ POR TANK SLOPE
IP3-CALC- 0217 Rev. 5 EC-32406 Markup Page 57 of 74 33 DIESEL GENERATOR FUEL OIL STORAGE TANK INCHES OIL vs. GALLONS OIL (CHART FOR DIP STICK INCH READING ONLY) 0v 0 500 1000 1500 2000 2500 3000 3W5O 4000 4500 5000 N 00 6M 6500 7000 7500 8000 GALLONS CURVE COMPENSATES FOR TAMK SLOPE
IP3-CALC- 0217 Rev. 5 EC-32406 Markup Page 58 of 74 33 DIESEL GENERATOR FUEL OIL STORAGE TANK TC-25D Rov. 0 mTTI I 6, 0IIC*
Vy ..
- m ~ dY.
INCHES OIL vs. GALLONS OIL Koc FV,, .
(CHART FOR LEVEL INDICATOR INCH READING ONLY) ___r,_"__a__ ________
Ir ThNE5PFE-o' am wVItymm or THt gmRSErFUEL Is nO.*'2 THMEN Tfe LE'VL rIDICATOA INCH FIF.ADIWN IWRIT BE ,OA1RIJECTO POR 5---
W.
110......
2 I ....
...-i*,0..... .. .. .
Inn 11./IJ w
10 500 1000 tA00 2000 2500 3000 360W 4000 4500 5000 5500 6000 66w) 7000 7100 BOD0 To COAMECT FOR S5P APPLY TH'E GALLONS POLLODiING.
cZOMECTED ACYW.A IWO, VIKADW IN4CH VALUE -~WIUVN 0 FIRON L-1-135 CURVE COMPENSATES FOfl TAWC SLOPE
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 59 of 74 ATTACHMENT 13 FAX MESSAGE, from A.E. Vazquez of Uehling, to R.F. Jones of MDM Engineering, "Certificate of Calibration" dated 12/18/95.
-u. S. :. - . . . . "-AEw I MM w
40 G~?3 "l "f P**-WL NJ 4USA Of4J PAML~I 04247Mz* PAX (201) W412oS Pass1. 'Lc RD.a 121631 TO: r.t,U m XWMD~t POINT VAX 914-739-6977 YAMI~I ALLE VkJSDt
=0'4M~ flgS1E1M3r oifmk FAiAMMR, pJ FAX 20 I-7Il-i2DS PaaW Fax NAA 7' L :oysL rGMfdC4rG. & 9 U* -40fy - f-I.SV* 6
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 60 of 74
~*' *-~ u~ ~ ci-
- - L.
1 rt.S .. ~ **'~* 2 Cr3Q.47; A.AJ. P~rLVN-
. L;.%Oi 11auo(2iý 7s; r7:0 FAXtZmIi na42imes 7 *aFcAur " 13 Onq.-S, :&9" Cfa-cec- C4- Af- &Wa jP7 CAenffcld 1 of afib9atc
- Now YOk ?ow Ainh,-ity F 0 W.$*,,4S t'mhhin ImtIum"am£suuw busby cee INhh LW thefMienwo gob"pc-%etw
-.mlwstw go tr*wiundimruiut mid y**VWt'ydc*Ar*1 iLkd by,t*
tL~mW aw with ftw4 Ackbplrt nas ts indkadns b4d usnt TAr boreC oDfih yrcx zMguwC tte af4 :t$ reaCsUMM;n IN ito '2r*.
Taltrnan dAfwd pmuicugmi>- ca~u s" n*ckNO rsikm isneqtitt frr t.e life gEtt nge prmwd &is ue for irs ciija- u*.*, puow c*,,ef WLmq ia.wp*a*w to ,niam 60 wing wshikc *',164 miaimm ," the
-Ww sale jmA~d. Lhr Omp uam3 l h'so.aJlb mraL~ pwpoma w impur-4i4muh qttdj ml M~ij~4 pv pi Cwfifie by &. &Vaz;uz
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 61 of 74 ATTACHMENT 14 Specification for "Liquid Level Switches", No. 9321-05-252-20, Revision 2, Paqes 3, 4, & 5, dated 9/19/95
,q '" IF r-O",;,F..4 7=-,FYI*.,
3- Dulas A.4aL- e" o C. DetaiL Eaquiran. tog DEiEP14glee -Type Cntrols:
1 1 ,,-illi
- Fue1 Ol Ipvar Tat so. 31 II-US Fuel 04 t ftaves Tl No,.Is 3 1 Wt-l2" fueL oil $tot*" Tmk #*. 23 4 I 1442L07S Vn Mt 47 Tak 00.
O W t Ron1? Fbel11 b Tookt ft 22 W-ILC~2095 FiaetOiI0oTWANk.fl
- t. The (*ltQvtnf aefortlmta Qppllwe to all tt4s. listed a*n!
FlWLd: Diesel rVel, Ile. I tNet oil, ceeroial grad.
%nftcG OMmiY: 9016 (tamW 0.1 - 1) ygecure: Atmeplorto Tamepnatwr.: 600 (Req. IS - 1109r)
"yPat OtmpIaeumench top sohetime "Fit, ickL 4 - US0 antem cul g lans" anecItion.
blepLL"er DOtair tLLcLeazici: A 4" ehebdida OS pipe (t.Bf tuh k..I inide diANEM ) *tsadgipeto wortL4 it All tants It dlestgn condlrll.um require dispLacerm atrle theta J1" Y diater, the vad shll hr
- tute tlu Next lerpet p ipae n1aiu6ed to cmucala cke dAoplacas mod Eunimb ~tzeaa-p6odL *s**.muaitq Iltupe.
Trim & DhLpLee KIear.lal: Suitable Mot service an4 ;oudittnw stat.4.
SwLLchos: Owl contact tirpa atnowt I whUy1 volt ASc.-L# ampe.
t
- 1. Tda lultowtq i*ufOqutm&p afqpl eao tW$te s4.c1, W43 lisqted he:;
Tnm .1 Contnl; Two level sta4., ban* ow dttetýiLl 6eah sctp.
Switch Ccsuce.; P.r.O.t.
switah *m*ium Yapglnoot, muitable in' OUECOO.S, Iilf, ixpsd es wtarh, With two eadUaltcoong les P. Eqwtpma snd Semitne to be Purathd bry the Seoler; TUe ite %aeLr 44sh ll tp, (abrict*t and detroLx tiquid *erel w*tcOt to
&ecmLtind la seetl4e 1-I-N ad 1-2-C.
3-. Squipart mod lrn*i to "he FIsLeid b" Othes:
- 1. Unhloa ng and listaLtntika at culpumemt.
- 1. MLSOV*I 9 fbp1*4 "d tri;.
Spe. No. 9)2L-26-ZZ.Z-2 Spec. Me. t321.Dt.2,ZO I'agpm I of
IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 62 of 74 dtcw'1.r
? .",, * 'y Ifl -cet- £&.n'
- i. Upper switch Actieni transfer on IsLitni 1niL, react a T1ta41 Level.
t'aqtcttonf-sl*n hqr t'&el retitil loUhr Switch At*lont transfer On tILi& latlt resat41 em Mii. lenl,
%* ~~FUngcL*&-lrmp evSL--&A, * '--,
- Oi~Diatom*ir zo Esak swottiaI to 4spae oviuh ct~uatLoa, taV41r7 (7 0iut*
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IP3-CALC-EG-00217 Rev. 5 EC-32406 Markup Page 64 of 74 ATTACHMENT 15 Telecopy transmittal Sheet IP3, To R. Jones (I&C), From M. Pactong (MECH ENG).
12/11/95 Ott*
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ATTACHMENT 9.1 DESIGN VERIFICATION COVER PAGE Sheet 1 of 1 DESIGN VERIFICATION COVER PAGE E] ANO-1 0 ANO-2 El IP-2 Z IP-3 E] JAF E] PLP FiiPNPS EJVY El GGNS []RBS LI W3 E] NP Document No. Revision No. Page I of 4 IP3-CALC-EG-00217. 5S
Title:
Emergency Diesel Generator Storage Tank Level Setpoints Z Quality Related [ Augmented Quality Related DV Method: [0 Design Review fl Alternate Calculation El Qualification Testing VERIFICATION REQUIRED DISCIPLINE VERIFICATION COMPLETE AND COMMENTS RESOLVED (DV print, sign, and date)
Eli Electrical Mechanical A Instrument and R. A. Schimpf/ See IAS Civil/Structural Nuclear Originator: B. Shepard/See IAS Be s Print/Sign//,9afe After Comments Hilve Been ResolVed EN-DC-134, Rev. 4
ATTACHMENT 9.6 DESIGN VERIFICATION CHECKLIST Sheet I of 3
'IDENTIFICATION: DISCIPLINE:
I Document
Title:
OCivil/Structural Emergency Diesel Generator Storage Tank Level Setpoints QElectrical
[] I&C Doc. No.:
Mechanical IP3-CALC.EG-00217 Rev. 5 QA Cat. SR 0 Nuclear R. A. Schimpf See )AS See IAS Other Verifier: Print Sign Date Manager authorization for supervisor performing Verification.
D3 N/A N/A Print Sign Date METHOD OF VERIFICATION:
Design Review 0 Alternate Calculations E] Qualification Test 0 The following basic questions are addressed as applicable, during the performance of any design verification. [ANSI N45.2.11 - 19741 [NP QAPD, Part 1I, Section 3][NP NQA-1-1994, Part II, BR 3, Supplement 3S- I].
NOTE The reviewer can use the "Comments/Continuation sheet" at the end for entering any comment/resolution along with the appropriate question number. Additional items with new question numbers can also be entered.
- 1. Design Inputs - Were the inputs correctly selected and incorporated into the design?
(Design inputs include design bases, plant operational conditions, performance requirements, regulatory requirements and commitments, codes, standards, field data, etc.
All information used as design inputs should have been reviewed and approved by the responsible design organization, as applicable.
All inputs need to be retrievable or excerpts of documents used should be attached.
See site specific design input procedures for guidance in identifying inputs.)
Yes 0 No 0 N/A 0
- 2. Assumptions - Are assumptions necessary to perform the design activity adequately described and reasonable? Where necessary, are assumptions identified for subsequent re-verification when the detailed activities are completed'? Are the latest applicable revisions of design documents utilized?
Yes J@ No 0 N/A [I
- 3. Quality Assurance - Are the appropriate quality and quality assurance requirements specified?
Yes 0 No E N/A [I EN-DC-134, Rev. 4
ATTACHMENT 9.6 DESIGN VERIFICATION CHECKLIST Sheet 2 of 3
- 4. Codes, Standards and Regulatory Requirements - Are the applicable codes, standards and regulatory requirements. including issue and addenda properly identified and are their requirements for design met?
Yes N No [] N/A 0
- 5. Construction and Operating Experience - Have applicable construction and operating experience been considered?
Yes 0 No 1 N/A U
- 6. Interfaces - Have the design interface requirements been satisfied and documented?
Yes 1@ No [ N/A 0
- 7. Methods - Was an appropriate design or analytical (for calculations) method used?
Yes 0 No 0 N/A 0
- 8. Design Outputs - Is the output reasonable compared to the inputs?
Yes 0 No 0 N/A 0
- 9. Parts, Equipment and Processes - Are the specified parts, equipment, and processes suitable for the required application?
Yes 0 No [I N/A 0
- 10. Materials Compatibility - Are the specified materials compatible with each other and the design environmental conditions to which the material will be exposed?
Yes 0 No 0 N/A 0 I1. Maintenance requirements - Have adequate maintenance features and requirements been specified?
Yes 0 No 0 N/A 0
- 12. Accessibility for Maintenance - Are accessibility and other design provisions adequate for performance of needed maintenance and repair?
Yes [I No [] N/A 0
- 13. Accessibility for In-service Inspection - Has adequate accessibility been provided to perform the in-service inspection expected to be required during the plant life?
Yes 0 No 0 N/A 0
- 14. Radiation Exposure - Has the design properly considered radiation exposure to the public and plant personnel?
Yes 0 No 0 N/A 0
- 15. Acceptance Criteria - Are the acceptance criteria incorporated in the design documents sufficient to allow verification that design requirements have been satisfactorily accomplished?
Yes 0 No 0 N/A 0 16, Test Requirements - Have adequate pre-operational and subsequent periodic test requirements been appropriately specified?
Yes CK No Q N/A 0 EN-DC-134, Rev. 4
ATTACHMENT 9.6 DESIGN VERIFICATION CHECKLIST Sheet 3 of 3
- 17. Handling, Storage, Cleaning and Shipping - Are adequate handling, storage, cleaning and shipping requirements specified'?
Yes E No 0 N/A 0
- 18. Identification Requirements - Are adequate identification requirements specified?
Yes 0 No 0 N/A 0 19, Records and Documentation - Are requirements for record preparation, review, approval, retention, etc.. adequately specified'? Are all documents prepared in a clear legible manner suitable for microfilniing and/or other documentation storage method? Have all impacted documents been identified for update as necessary?
Yes 0 No 0 N/A 0
- 20. Software Quality Assurance- ENN sites: For a calculation that utilized software applications (e.g., GOTHIC, SYMCORD), was it properly verified and validated in accordance with EN- IT-104 or previous site SQA Program?
ENS sites: This is an EN-IT-104 task. However, per ENS-DC-126, for exempt software, was it verified in the calculation?
Yes [I No 0 N/A 0
- 21. Has adverse impact on peripheralcomponents and systems, outside the boundary of the document being verified, been considered?
Yes 0 No 0 N/A 0 EN-DC-134, Rev. 4
ATTACHMENT 9.7 DESIGN VERIFICATION COMMENT SHEET Sheet I of I Comments / Continuation Sheet EN-DC-134, Rev. 4